Membrane Potential and Firing Rate in Cat Primary Visual Cortex
hv1电压门控质子通道
hv1电压门控质子通道英文回答:Hyperpolarization-Activated Cyclic Nucleotide-Gated (HCN) Ion Channels.Hyperpolarization-activated Cyclic Nucleotide (HCN) ion channels belong to the voltage-gated ion channel familythat are activated by hyperpolarization (a more negative shift in membrane potential). They play a crucial role in the electrical properties of excitable tissues,particularly in regulating the heart rate and maintaining the rhythmic firing of neurons.HCN channels are gated by a transmembrane voltage sensor and are modulated by cyclic nucleotides, such as cyclic adenosine monophosphate (cAMP) and cyclic guanosine monophosphate (cGMP). When the membrane potential is hyperpolarized, the voltage sensor undergoes a conformational change that opens the pore of the channel,allowing sodium ions to flow into the cell. The activation of HCN channels leads to a decrease in the excitability of the cell, as the influx of positive ions reduces the hyperpolarization of the membrane.HCN channels are classified into four subtypes (HCN1-HCN4), which exhibit distinct biophysical properties and tissue-specific expression patterns. They are found in various tissues throughout the body, including the heart, brain, and sensory organs.In the heart, HCN channels contribute to the pacemaker activity of the sinoatrial (SA) node, which is responsible for initiating the heart beat. HCN channels in the SA node generate a slow inward current, known as the If current, that spontaneously depolarizes the cell membrane and triggers an action potential. The If current is modulated by the autonomic nervous system, which allows for the regulation of heart rate in response to physiological cues.In the brain, HCN channels are involved in the generation of rhythmic oscillations in neural circuits.They are expressed in the thalamus, hippocampus, and cortex, where they contribute to theta and gamma oscillations,which are associated with cognitive functions such as memory and attention. HCN channels also play a role in the regulation of synaptic plasticity, which is essential for learning and memory.Dysfunction of HCN channels has been implicated in a number of neurological and cardiac disorders. Mutations in HCN genes have been linked to diseases such as epilepsy, autism spectrum disorder, and cardiac arrhythmias. Understanding the molecular mechanisms underlying HCN channel function is therefore of great clinical importance.中文回答:电压门控质子通道。
[精选]第22章抗心律失常药--资料
苯妥英钠 phenytoin sodium 1. 作用与lidocaine 相似; 2. 用于室性心律失常; 3. 与强心苷竞争Na+-K+-ATP酶
治疗强心苷中毒的室性心律失常首选。
普萘洛尔 propranolol
1. ↓窦房结、普氏纤维自律性; 2. ↓房室传导; 3. ↑房室结 ERP; 4. 主要用于室上性及交感兴奋所致各种
Na+内流↑, K+外流↓ Ca2+内流↑,K+外流↓
automaticity↑
最大舒张电位负值↓ 阈电位负值↑
自动除极速度↑
自律性↑
快速心律失常
2 . Afterdepolarization (后除极) 心肌细胞在一个AP后产生一个提前的除极化 。
早后除极 ( Early afterdepolarization, EAD ) 发生在2、3相中,由Ca2+内流↑引起。
§2 Mechanism of Arrhythmia 心律失常发生机制
1. Automaticity (自律性)↑
(maximal diastolic potential , MDP)
阈电位 (threshold potential , TP)
4相自动去极化速度 (为主)
(spontaneous depolarizing speed of phase 4)
心律失常;窦性心动过速首选。
胺碘酮 amiodarone (安律酮) 1. 明显延长APD、ERP; 2. 广谱抗心律失常。
维拉帕米 verapamil(异搏定 isoptin) 1. ↓窦房结自律性, ↓房室传导; 2. ↑窦房结、房室结ERP; 3. 用于室上性心律失常
聚醚砜膜改性 国外
Hydrophilic modification of poly(ether sulfone)ultrafiltration membrane surface by self-assembly of TiO 2nanoparticlesMing-Liang Luo a ,*,Jian-Qing Zhao a ,Wu Tang b ,Chun-Sheng Pu caCollege of Materials Science and Engineering,South China University of Technology,Guangzhou 510640,ChinabLASMIS,University de Technologie de Troyes,Troyes Cedex 10010,France cCollege of Petroleum Engineering,Xi’an Shiyou University,Xi’an 710065,ChinaReceived 1June 2004;received in revised form 17November 2004;accepted 17November 2004Available online 25December 2004AbstractMembrane fouling is one of the major obstacles for reaching the ultimate goal,which realizes high flux over a prolonged period of ultrafiltration (UF)operation.In this paper,TiO 2nanoparticles of a quantum size (40nm or less)in anatase crystal structure were prepared from the controlled hydrolysis of titanium tetraisopropoxide and characterized by X-ray diffraction (XRD)analysis and transmission electron microscopy (TEM).The hydrophilic modification of poly(ether sulfone)UF membrane was performed by self-assembly of the hydroxyl group of TiO 2nanoparticle surface and the sulfone group and ether bond in poly(ether sulfone)structure through coordination and hydrogen bond interaction,which was ascertained by X-ray photoelectron spectroscopy (XPS).The morphology and hydrophilicity were characterized by scanning electron microscopy (SEM)and contact angle test,respectively.The composite UF membrane was also characterized in terms of separation behavior for polyethylene glycol-5000solute.The experimental results show that the composite UF membrane has good separation performance and offers a strong potential for possible use as a new type of anti-fouling UF membrane.#2004Elsevier B.V .All rights reserved.Keywords:Ultrafiltration;Self-assembly;Anti-fouling membrane;TiO 2nanoparticles;Hydrophilicity1.IntroductionIn recent years,more and more attention in ultrafiltration (UF)membrane has been attracted for a variety of applications in waste-water treatment,substance separation,solute concentration,and so on.The major drawback in the extensive use of membranes includes membrane fouling,which results in flux decline during operation [1].Several types of fouling could occur in the membrane system,e.g.crystalline fouling,organic fouling,particulate and colloidal fouling,and microbial fouling,etc.[2].Many approaches to control membrane fouling have been performed,which generally involve pretreatment of the feed solution,surface modification of the membrane (like hydrophobic or hydrophilic and/locate/apsusc*Corresponding author.Tel.:+862087113576;fax:+862087113576.E-mail address:yfsailing_wxg@ (M.-L.Luo).0169-4332/$–see front matter #2004Elsevier B.V .All rights reserved.doi:10.1016/j.apsusc.2004.11.054electronegative or electropositive modification),opti-mization of module arrangement and process condi-tions,and periodic cleaning[3,4].Even after the development for decades,particulate and colloidal fouling still remains the main reason forflux decline in the process of industrial wastewater treatment[3,5].Poly(ether sulfone)(PES)is a kind of special engineering plastics with good performances.The structure of PES used in the paper was shown in Fig.1. It can be imagined that PES has crystalline to some degree because of harder benzene ring and softer ether bond existed in the structure.PES possesses many good performances such as high mechanical property and heat distortion temperature,good heat-aging resistance,environmental endurance and processing. It has become one of important separation membrane materials,but its hydrophobicity controlled by PES structure leads to low membraneflux and fouling easily,which has greatly effect on applicationfield and usage life of separation membrane.It is necessary to modify PES membrane surface by physical and chemical methods and improve its hydrophilicity. Recently,modification methods of UF membrane involve ultraviolet irradiation[6],graft polymeriza-tion[7,8],glow discharge[9],and ozone[1,10,11]on membrane surface,and so on.The hydrophilicity and anti-fouling capability of UF membrane increase to some degree,but some of them are complicated and it is difficult to control the hydrophilicity of membrane, others may make some performances of UF membrane loss.A new approach to modify PES ultrafiltration membrane by self-assembly of TiO2nanoparticles is presented in this paper.Titanium dioxide(TiO2)has been the focus of numerous investigations in recent years,because its high hydrophilicity[12,13],stable chemical property, innocuity and low cost,etc.Most of researches carried out in thisfield have focused on the use of TiO2 powder suspended in the water as a catalyst[14].The method of TiO2self-assembly on the surface with the terminal functional groups(for example,single-crystal silicon,quartz,and glass substrates)has been used to fabricate multilayer ultrathinfilms[15–17]. The self-assembly behavior of TiO2on the surface of polymer with COOH,SO2OH,sulfone group and ether bond may be explained by two different adsorption schemes.One scheme is that TiO2was bound with oxygen atoms of these groups via coordination to Ti4+cations.The other scheme is to form a hydrogen bond between these groups and the hydroxyl group of TiO2surface[18].Thus,it is probable to self-assemble the TiO2nanoparticles on membrane sur-face.In this paper,TiO2nanoparticles were prepared from the controlled hydrolysis of titanium tetraiso-propoxide.The particle structure and size were characterized by X-ray diffraction(XRD)analysis and transmission electron microscopy(TEM).The composite UF membrane was prepared by self-assembly of TiO2on the membrane surface.X-ray photoelectron spectroscopy(XPS)was performed with the UF-tested membrane after the actual UF operation conditions.The morphology and hydrophilicity of composite UF membrane were characterized by scanning electron microscopy(SEM)and contact angle test,respectively.The composite ultrafiltration membrane was also characterized in terms of separa-tion behavior for polyethylene glycol-5000solute.The anti-fouling and fouling mitigation of the composite UF membrane was examined and verified.2.Experimental2.1.Preparation of the nanosized TiO2particlesTiO2nanoparticles were prepared from the con-trolled hydrolysis of titanium tetraisopropoxide at acidic condition[19].A 1.25ml sample of Ti(OCH(CH3)2)4(AR;Chengdu Unite-chemcial Company,China)dissolved in25ml of absolute ethanol was dropped to250ml of distilled water (48C),adjusted to pH1.5with hydrochloric acid under vigorous stirring.After this mixture was stirred overnight,a transparent colloidal suspension was obtained.Powdered sample was obtained by evapor-ating(358C)using a rotavapor and by drying(508C) under vacuum.The gel powder was annealed in muffle furnace at5008C and the nanosized TiO2particles were obtained.M.-L.Luo et al./Applied Surface Science249(2005)76–8477 Fig.1.Molecular structure of the PES.2.2.Preparation of PES/TiO2compositeultrafiltration membranesThe PES ultrafiltration membrane was made via phase inversion method[20].The UF membrane was rinsed in a sodium carbonate solution(0.2wt.%)and then washed with distilled water.The neat PES membrane with an area of38.5cm2was dipped in the transparent TiO2colloidal solution,stirred for1min by ultrasonic method and placed for1h to deposit TiO2nanoparticles on the membrane surface and then washed with distilled water.2.3.Characterization2.3.1.Characterization of the nanosized TiO2 particlesThe crystal structure of TiO2nanoparticle was characterized by X-ray diffraction(XRD).XRD analysis was performed on TiO2powder samples with a PHI-5400X-ray diffractometer using18kW Cu K a(l=0.15418nm)radiation.The particle size was determined by a JEOL transmission electron micro-scope(TEM,JEOL JEM-200CX)at120kV.For the TEM observation,TiO2powder in distilled water solution(0.5g lÀ1)was dropped on a carbon-coated grid and then dried at room temperature.2.3.2.Characterization of the PES/TiO2composite UF membraneThe surface topologies of the PES membrane containing TiO2nanoparticle were investigated with a JSM-5800scanning electron microscope(SEM).The surface morphology of the neat PES membrane was also examined and was compared with that of the TiO2 self-assembled version.For the SEM observation,the membrane samples were cut into appropriate sizes and the surfaces were coated with platinum or gold by a sputter coating machine.The pore size distribution of composite membrane was measured by mercury displacement method with Autopore9220II aperture-testing meter.X-ray photoelectron spectroscopy(XPS)was performed on the surface of composite membrane with a PHI-5400spectrometer using Mg K a X-ray (1253.6eV).The X-ray gun was operated at10kVand 1mA.The spectra were taken at the takeoff angle (defined as the angle between the detected photoelec-tron beam and the membrane surfaces)of458to give a sampling depth of ca.2.3nm.The sensitivity factors of individual elements for quantitative analyses were taken with the values from the standard vision library provided by the manufacturer,which were based on a combination of photoelectric cross-section,transmis-sion function,and inelastic mean free path.Static contact angles of the composite membrane surface were measured using the captive air bubble technique.Membranes were inverted in deionized water and air bubbles were placed in contact with the surface. The static angle was measured using an Eromag-1 contact angle testing apparatus.The contact angle was determined from the average value of10-times measurements and the measurement error wasÆ38.2.3.3.Separation performance of the PES/TiO2 composite UF membraneThe mass transfer characteristics of UF membrane for200ppm polyethylene glycol(PEG-5000)aqueous solution were determined in laboratory at0.2MPa, 258C for30min with the apparatus of a continuous flow type.The waterflux was calculated by direct measurement of the mass of the permeateflow:J¼V=At(1) where J is the membraneflux(L mÀ2hÀ1),V the permeate volume(L),A the membrane area(m2) and t the ultrafiltration time(h).The solute rejection was defined as follows:R¼ð1Àc p=c fÞÂ100%(2) where R is the solute rejection,c f the feed concentra-tion,c p the permeate concentration.3.Results and discussion3.1.Crystal structure and size of synthesized TiO2 nanoparticleFig.2shows the X-ray diffraction spectrum of TiO2 particles.The synthesized particles are composed entirely of anatase compared with those reported for rutile(110)(2u of27.458)and anatase(101) (25.248)[21].The particle size is determined by transmission electron microscopy(TEM)explicitly. The particles size is about5–42nm(Fig.3).M.-L.Luo et al./Applied Surface Science249(2005)76–84 783.2.Microstructure and pore size distribution of the composite membraneThe microstructure of the composite membrane is shown in Fig.4.As shown in Fig.4a (SEM of the composite membrane cross-section),the sectional structure of composite membrane has asymmetry and many smaller pores,which shape looks like the finger,are filled in the membrane.When the dope solution is coated on the smooth glass plate,the pore size formed towards the air is smaller due to the solution evaporation,but the pore size formed towards the glass plate is larger because the exchange happened quickly between the solvent phase and the non-solvent phase and immediately phase inversion starts and after few minutes thin polymeric composite film separated out from the glass.Fig.4b and c are the SEM graphs of the membrane surface before and after treated by TiO 2colloidal solution,respectively.The neat PES mem-brane has the typical surface morphology of a characteristic ridge-and-valley structure (Fig.4b),but the ridge-and-valley structure is not so visible.Fig.4c displays the surface morphology of the TiO 2self-assembled composite membrane,where TiO 2nanoparticles appear to exist as nodular shapes of ca.40nm or less on the surfaces of the ridges and the membrane surface has clear ridge-and-valley struc-ture.The pore size distribution of the composite membrane is shown in Fig.5.As shown in Fig.5,the composite membrane has narrow pore size distribution,small pore size and average pore size 27.1nm.3.3.Surface characterization of the composite membraneTo con firm the self-assembly TiO 2nanoparticles on the composite membrane surface and further to estimate the abrasive resistance of the membrane surface,X-ray photoelectron spectroscopic (XPS)analyses were carried out for the PES/TiO 2composite membrane treated under various conditions.The constituent elements of the composite membrane surface are hydrogen,carbon,oxygen,sulfur,chlorine,and titanium.Thus,XPS analyses were performed on the elements of carbon,oxygen,sulfur,chlorine,and titanium,but not on hydrogen because its photoelec-tron cross-section was too small to be characterized by XPS.The core-electron binding energies of the constituent elements are typically 287eV (C 1s),537eV (O 1s),23eV (O 2s),229eV (S 2s),270eV (Cl 2s),199eV (Cl 2p)and 458eV (Ti 2p)[22].Fig.6shows the resulting spectrum,in which all the photoelectron peaks appear at positions similar to the above values and the presence of Ti peaks.The results provide evidence of TiO 2self-assembly on the composite membrane surface.On the basis of the observed photoelectron peaks and corresponding sensitivity factors,the relative atomic concentrations of the individual elements can be calculated:C i ¼A i =S iP mj A j =S j(3)where A i is the photoelectron peak area of the element i ,S i the sensitivity factor for the element i ,and m theM.-L.Luo et al./Applied Surface Science 249(2005)76–8479Fig.2.XRD spectrum of the synthesized TiO 2.Fig.3.TEM micrograph of the TiO 2nanoparticles.number of the elements in the sample.In Table 1,the elemental compositions determined by an angle-resolved XPS analysis were summarized for the com-posite membranes with different washing conditions and UF operation time.There was an initial drop in the relative atomic concentration of Ti element after washing the composite membrane,which had been just formed from dipping into the TiO 2colloidal solution.An additional loss of TiO 2nanoparticles was observed upon further UF operation with run time of 3h.The UF process was operated in the cross-flow mode where the feed solution was pumped across the composite membrane parallel to its surface.It was found that TiO 2particles were wiped out after 3h UFM.-L.Luo et al./Applied Surface Science 249(2005)76–8480Fig.4.SEM micrographs of the UF membrane:(a)cross-section;(b)neat surface;(c)surface treated by TiO 2colloidalsolution.operation and thought the loosely bound TiO2parti-cles cannot overcome the shear force.However,the TiO2loss did not continue to progress as the UF operational time increased more,and the amount of TiO2leveled-off after10h of UF operation.This result indicates that a considerably substantial amount of TiO2nanoparticles remains tightly bound on the surface of the membrane under actual UF running conditions,which is expected to improve the hydro-philicity of PES membrane and prevent from the membrane fouling.3.4.Design of TiO2nanoparticle self-assembled composite membraneTiO2nanoparticle in the anatase form is very hydrophilic,photoactive and practical for the wide-spread environmental applications such as water purification,wastewater treatment,hazardous waste control,air purification,and water disinfection [19,23,24].In this research,composite UF membrane was devised by the self-assembly between TiO2 nanoparticle and polymer with the ether bond and sulfone group(Fig.7)because of the strong electronegative of oxygen in the ether bond and sulfone group of the PES.As UF process was operated in the cross-flow mode under high pressure,simply adsorbed particles may be detached from membrane surface.XPS results in Table1indicate that some TiO2 particles in composite membrane have a sufficient binding strength for the actual operation,which agree with other researches on the interaction behavior of TiO2nanoparticle[18,25].It is concluded that a novel organic–inorganic membrane is successfully prepared by self-assembly process.3.5.Hydrophilicity and UF performance of the composite membraneThe hydrophilic and separation performance of the membrane surface untreated and treated by TiO2 colloidal solution are presented in Table2.The area of UF membrane is38.5cm2,applied pressure 0.2MPa,operational temperature258C and feed concentration200ppm(PEG-5000)in this experi-ment.As shown in Table2,the contact angle of the membrane treated by TiO2colloidal solution become small and theflux and the retention increase greatly.M.-L.Luo et al./Applied Surface Science249(2005)76–8481Fig.6.XPS spectra of the elements on the composite membrane. Table1Elements compositions of the PES/TiO2composite membrane undervarious washing conditions and UF operational timeSample a Takeoff angle(8)Relative atomic concentration(%)C O S Ti Cl14543.9530.8810.77 5.728.6824541.8032.8410.77 5.169.4334540.9534.5210.97 3.589.9844540.9534.5410.97 3.569.98a Analyses were performed for the TiO2self-assembled UFmembranes(1)just after preparation,(2)after washing withflowingwater,(3)after UF operation of3.0h,(4)after UF operation ofanother10.0h.The initial structure of the UF membrane is changed due to the self-assembly of TiO 2nanoparticles and the ridge-and-valley structure on the membrane surface is more clear.The roughness of the membrane surface increases.Generally,the hydrophilicity of membrane surface increases with the increase of roughness [26].On the other hand,the hydroxylcontent of membrane surface increases due to incorporate TiO 2nanoparticles into membrane sur-face.The hydroxyl is polarity and can interact well with water molecules through van der Waals ’force and hydrogen bond.So the probability of water permeated through the composite membrane enhances and the probability of PEG-5000permeated through the composite membrane drops off.Fig.8shows that the fluxes of the neat PES membrane and the treated PES membrane vary with time.As seen in Fig.8,the PES membrane treated by TiO 2colloidal solution always keeps higher flux.This experimental result shows that the anti-fouling performance of the PES ultra filtration membrane is improved remarkably due to TiO 2nanoparticles self-assembly.A strong potential for possible use as a new type of anti-fouling UF membrane is offered.M.-L.Luo et al./Applied Surface Science 249(2005)76–8482Fig.7.Mechanism of self-assembly of TiO 2nanoparticles:(I)by a coordination of sulfone group and ether bond to Ti 4+;(II)by a H-bond between sulfone group and ether bond and surface hydroxyl group of TiO 2.Table 2Contact angle and UF performance of membrane Sample a Contact angle (8)Flux (L m À2h À1)Retention (%)539.670.221.9619.2102.934.5aAnalyses were performed for (5)the neat and (6)the TiO 2self-assembled UF membranes.4.ConclusionsMembrane fouling by hydrophobic substances has been known to be the main cause to deteriorate the UF performance of PES membranes.It was developed that a new type of composite membrane as an approach to solve fouling problem.Its anti-fouling effect was characterized.The TiO2nanoparticle of a quantum size(40nm or less)in anatase form was prepared by the controlled hydrolysis of titanium tetraisopropoxide.The particle structure and size were characterized by X-ray diffraction(XRD)analysis and transmission electron microscopy(TEM).TiO2 nanoparticles were incorporated onto the poly(ether sulfone)membrane surface by self-assembly.X-ray photoelectron spectroscopy(XPS)demonstrated quantitatively that TiO2particles were tightly self-assembled with a sufficient bonding strength for the actual UF process.The contact angle test of the composite membrane shows that the hydrophilicity of the membrane surface improves remarkably.The fouling experiment verified a substantial prevention of the composite membrane against the hydrophobic substances fouling,suggesting a possible use as a new type of anti-fouling composite membrane. AcknowledgementsThe authors wish to acknowledge thefinancial support from the National Basic Research Program-2001CB-2091grant for this project.Thanks are also due to Environmental Science Research Institute, Chinese Academy of Sciences for supplying us with the PES membrane and Xi’an Modern Chemistry Research Institute for access to the XRD,XPS,TEM and SEM equipments.We also would like to thank Prof.Fengji LU for many valuable discussions. 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[13]Q.Hu,Fabrication and characterization of poly(amide-imide)/TiO2nanocomposite gas separation membranes,Ph.D.Thesis,Virginia Polytechnic Institute and State University, 1997.[14]T.Matsunaga,R.Tomoda,T.Nakajima,N.Nakamura,T.Komine,Continuous-sterilization system that uses photosemi-conductor powders,Appl.Environ.Microbiol.54(1988)1330.[15]Y.Liu,A.Wang,R.Claus,Molecular self-assembly of TiO2/polymer nanocompositefilms,J.Phys.Chem.B101(1997) 1385.[16]R.Rizza,D.Fitzmaurice,Self-assembly of monolayers ofsemiconductor nanocrystallites,Chem.Mater.9(1997)2969.[17]N.Kovtyukhova,P.J.Ollivier,S.Chizhik,A.Dubravin,E.Buzaneva,A.Gorchinskiy,A.Marchenko,N.Smirnova,Self-assembly of ultrathin composite TiO2/polymerfilms,Thin Solid Films337(1999)166.[18]S.J.Lee,S.W.Han,M.Yoon,K.Kim,Adsorption character-istics of4-dimethylaminobenzoic acid on silver and titania: diffuse reflectance infrared Fourier transform spectroscopy study,Vib.Spectrosc.24(2000)265.[19]W.Choi,A.Termin,M.R.Hoffmann,The role of metaliondopants in quantum-sized TiO2:correlation between photo-reactivity and charge carrier recombination dynamics,J.Phys.Chem.98(1994)1366.[20]M.Luo,Preparation and characterization of polyethersulfone/TiO2nanoparticles composite ultrafiltration membrane with high hydrophilicity and its pollution mechanisms,Ph.D.The-sis,Xi’an Jiaotong University,2003.M.-L.Luo et al./Applied Surface Science249(2005)76–8483[21]J.Lima-de-Faris,Structural Mineralogy,Kluwer AcademicPublishers,Dordrecht,1994.[22]J.Wang,W.Wu,Q.Zhao,Electron Spectroscopy,NationalDefence Industry Press,Beijing,1992.[23]M.R.Hoffmann,S.T.Martin,W.Choi,D.W.Bahnemann,Environmental application of semiconductor photocatalysis, Chem.Rev.95(1995)69.[24]ls,R.H.Davies,D.Worsley,Water purification bysemiconductor photocatalysis,Chem.Soc.Rev.22(1993)417.[25]ls,S.L.Hunte,An overview of semiconductor photo-catalysis,J.Photochem.Photobiol.A:Chem.108(1997)1.[26]J.Yu,X.Zhao,Q.Zhao,Effects of surface morphology ofphotocatalytic porous TiO2thinfilms on hydrophilicity,J.Chin.Ceram.Soc.3(2000)245.M.-L.Luo et al./Applied Surface Science249(2005)76–84 84。
Action potential nerve conduction动作电位与神经传导-文档资料
Action Potential Conduction
F8-19
• Movement of the AP along the axon at high speed is called conduction. • A wave of action potentials travel down the axon. • Each section of the axon is experiencing a different phase of the AP (see figure).
Terminology Associated with Changes in
F8-7, F8-8
Membrane Potential
• Depolarization- a decrease in the potential difference between the inside and outside of the cell.
•Hyperpolarization- an increase in the potential difference between the inside and outside of the cell.
• Repolarization- returning to the RMP from either direction.
Graded Potential vs Action Potential
Timecourse of the Action Potential
Na+ Channels Have Two Gates
F8-15
• The movement of the inactivation gate is coupled to the movement of the activation gate, but its response time is slower. • When the activation gate is open, the signal passes along the channel protein to the inactivation gate.
生理学的概念及生命活动的特征5
Resting membrane potential
Resting membrane potential
■ is expressed as the measured potential difference across the cell membrane in millivolts(mV).
■ is, by convention, expressed as the intracellular potential relative to the extracellular potential. Thus, a resting membrane potential of –70 mV means 70 mV, cell negative
Resting membrane potential The three conditions of Establishment of resting membrane potentials
Resting membrane potential
Formation process
The resting membrane potential is established by diffusion potentials
B, Establishment of a diffusion potential when the nerve fiber membrane is permeable only to sodium ions. Note that the internal membrane potential is negative when potassium ions diffuse and positive when sodium ions diffuse because ofopposite concentration gradients of these two ions.
superFlashMemory
The split-gate memory cell size is comparable to traditional stacked gate memory cells using the same process technology. This is possible because
1. the tunneling injector cell does not need the extra spacing to isolate the higher voltages and currents required for programming the stacked gate array, and
Membrane Potential - Mount Vernon School District膜电位-弗农山校区
▪ Measured in millivolts (mV)
▪ Requires active transport (Na+/K+ pump) to maintain
ATP -> ADP + Pi
Primary Active Transport
Membrane Potential
▪ The voltage across the plasma membrane that is the result of a difference in electrical charge inside vs e the cell
Membrane Potential
2019-13
QUICK REVIEW
This is an example of what kind of transport?
Passive (Simple Diffusion)
This is an example of what kind of transport?
ATP -> ADP + Pi
Less K+ leaks out because it is attracted to the negative charge inside the cell
The Na+/K+ pump controls the leak… and does exactly opposite 3 Na+ out and 2K+ in
神经电生理学
R – gas constant T – absolute temperature
C1 WC 2.3RT log C2
WE qV zFV
F – Faraday’s constant V –potential difference z - valence number of the ion
VNa
[ Na ]out 58log mV [ Na ]in 120 mV 58mV 12
58log
[Cl ]in VCl 58log mV [Cl ]out 58log 5 mV 81mV 125
The membrane potential
The membrane potential is the weighted average of each contributing ion's equilibrium potential. Millman equation:
Action potential
Action potential (AP) is a transient depolarizatinon of the membrane potential. Early experiments (K.C. Cole i H. J. Curtis, 1939) showed that the membrane becomes almost 50 mV positive inside at the peak of the AP. If the AP was due to transient breakdown in permeability to all ions, it would depolarize membrane to zero, but not beyond. Experiments on AP generation mechanism were performed on on the squid giant axon, which is up to 1 mm in diameter. It provided a great experimental advantage as it allowed to insert voltage clamp electrodes inside the axon. Loligo pealei
生理学——细胞的生物电现象
gradients across membrane and diffusion force.
二、动作电位的产生机制 Formation mechanism of action potential
The difference in electrical potential across the membrane of an undisturbed cell, having a positive sign on the outside surface and a negative sign in the interior.
(2) Na+通道的迅速失活及电压门控K+通道的 开放,是动作电位复极化的主要原因。
(3) Na+- K+泵的活动,使Na+、 K+重新回到 原来的分布状态。
☆负后电位的形成原因
复极时,迅速外流的K+蓄积在膜的外侧, 暂时性阻碍了K+的外流
☆正后电位的形成原因
生电性Na+- K+泵的活动
三、兴奋的引起和兴奋的传导机制
An action potential is a rapid change in the membrane potential. Each action potential begins with a sudden change from the normal resting negative potential to a positive membrane potential (depolarization) and then ends with an almost equally rapid change back to the negative potential (repolarization).
膜电容去离子法海水淡化装置单元脱盐过程的数值模拟
Vol. 42, No. 6Jun., 2020第42卷第6期2020年6月舰船科学技术SHIP SCIENCE AND TECHNOLOGY膜电容去离子法海水淡化装置单元脱盐过程的数值模拟肖民,金苗苗,姚寿广(江苏科技大学能源与动力学院,江苏镇江212003)摘 要:本文针对一种基于中部流入式的膜电容法脱盐装置组件,建立了脱盐单元的三维瞬态分析模型。
在 对模拟结果线性回归拟合验证了该模型适用性基础上,对脱盐单元进行了数值模拟分析。
结果表明:随着入口孔径的增大,MCDI 脱盐单元的出口最低浓度升高,而出口最高浓度降低;且入口孔径越大,其达到吸附饱和的时间越长,但吸附效率越小,脱附时间也相应增加,脱附效率能够达到的峰值也越大;同一入口孔径条件下,反接脱附方 式下能够达到的最高出口浓度均高于短接方式。
关键词:膜电容去离子;中部流入型;数值模拟中图分类号:U664.591 文献标识码:A文章编号:1672 - 7649(2020)06-0110-05 doi : 10.3404/j.issn,1672 - 7649.2020.06.022Numerical simulation of desalting process in seawater desalination plant bymembrane capacitive deionizationXIAO Min, JIN Miao-miao, YAO Shou-guang(School of Energy and Power Engineering, Jiangsu University of Science and Technology, Zhenjiang 212003, China)Abstract: Based on the middle inflow type desalting module in membrane capacitance method, a three-dimensionaltransient analysis model of desalting unit was established. Then the applicability of the model was verified by linear regres sion fitting of simulation results, and the desalting unit was analyzed by numerical simulation. The results show that with the increase of inlet aperture, the minimum outlet concentration of M CDI desalting unit increases, while the maximum decreases.The larger the inlet aperture, the longer the desalting unit reaches the adsorption saturation time, and the smaller the adsorp tion efficiency, yet the more the desorption time increases, and the higher the desorption efficiency peak. Under the same in let aperture, the maximum outlet concentration in reverse desorption mode both achieves higher than that in short.Key words: membrane capacitive deionization ; middle inflow type ; numerical simulation0引言电容去离子技术(Capacitive Deionization , CDI ) 类似但又区别于超级电容器一現其在流通模式下运行,并且侧重点在于脱盐而不是电荷存储。
Membranepermeability
387AddressDepartement Recepteurs et Proteines Membranaires, UPR 9050 CNRS, Ecole Superieure de Biotechnologie de Strasbourg, Rue Sebastien Brant, F-67400 Illkirch, FranceCurrent Opinion in Cell Biology2001, 13:387–3880955-0674/01/$ — see front matter© 2001 Elsevier Science Ltd. All rights reserved.The increased availability of information from several genomes, including quite recently the human genome, and the development of new high throughput techniques to study expression patterns and protein–protein interactions have accelerated the pace of discoveries in cell biology. But at the same time this wealth of information is obscuring our understanding of biological processes such as cell membrane permeability and their regulation. There is a clear need to classify, assemble and integrate all this infor-mation to obtain a clearer picture on the role of ions and other small molecules in key cellular functions. Membrane permeability to ions and small molecules involve three major classes membrane proteins: trans-porters, channels and pumps. These three classes will be addressed in this section of Current Opinion in Cell Biology. In the first review, Daniel van Belle and Bruno André pre-sent (pp 389–398) their genomic analysis and personal view of yeast membrane transporters following the sequencing of the genome of Saccharomyces cerevisiae. 6% of the proteome is directly involved in transport of small mol-ecules across membranes in yeast (transportome) and only half of the transporters have been assigned a function. T wo major features of the transportome from yeast are worth mentioning: the growing numbers of transporters found in intracellular membranes and the function of transporter homologues as sensors for external nutrients. Van Belle and André are quite optimistic about the likehood of deci-phering the functions of all individual proteins of the entire transportome, but the main challenge remains to understand how the transporters from the intracellular organelles work together with those from the cytoplasmic membrane and how they are regulated to ensure home-ostasis in yeast.A global picture of a particular aspect of ion homeostasis in plants, the response to salt stress, is emerging owing to recent advances with two model systems, the plant Arabidopsis thaliana and the yeast S. cerevisiae. Soil salinity is a major abiotic stress in plant agriculture worldwide. This has led to research into salt tolerance with the aim of improving crop plants. Ramón Serrano and Alonso Rodriguez-Navarro (pp 399–404) in the second review discuss the mechanism by which plant cells regulate cation fluxes at the level of both the cytoplasmic and the tono-plast membrane to maintain ion homeostais in response to salt stress and to minimise the toxic effects of Na+uptake. The conservation of many actors in ion homeostasis between fungi and plants makes the yeast S.cerevisiae a model system of considerable value. Some of the major Na+extrusion transporters of plant tonoplast and plasma membrane have been identified, and it was shown that Na+uptake is regulated by modulators of membrane potential that regulate proton pumps, K+transporters and uncoupling proteolipids. Ca2+signals and kinases are other key components of the signal transduction pathways medi-ating the regulation of plant transporters.Programmed cell death culminating in apoptosis is essen-tial for normal tissue homeostasis and has increasingly been implicated in mediating pathological cell loss. Although apoptosis of cells is accompanied by characteris-tic morphological changes, including cell volume loss and thus changes in membrane permeability to water and ions, it was not clear whether intracellular changes of ion home-ostasis was a passive secondary feature of the cell death or a driver of the process. Recent evidence shows that apop-totic volume decrease (AVD) occurred early, before characteristic ultrastructural or biochemical events (cytochrome release or caspase activation) and that changes in ion concentrations may inhibit or promote apoptosis. In their review, Shan Ping Yu, Lorella Canzoniero and Dennis Choi (pp 405–411) discuss the cur-rent status of knowledge of the role of mainly Ca2+and K+ ions as modifiers or mediators of the apoptotic cascade.. When a new membrane protein structure appears in the lit-erature this rare event is celebrated in the structural biology community and obviously a review article in Current Opinion in Structural Biology will follow. So why publish a review in Current Opinion in Cell Biology in a section devoted to mem-brane permeability? Simply because cell biologists have a lot to learn from the T olC structure and from understanding its function. The resolution of this structure has clearly removed a conceptual barrier to interpretation of diverse mutational data on the role of T olC and T olC-related pro-teins in secretion of toxins and efflux of toxic chemicals by gram negative bacteria. In their review Christian Andersen, Colin Hughes and Vassilis Koronakis (pp 412–416) describe how T olC assembles as a channel-tunnel (a “chunnel”according to Kathleen Postle and Hema Vakharia), which crosses the Escherichia coli outer membrane and the periplas-mic space and how this structure suggests a mechanism for secretion and efflux of molecules across two membranes which by-pass the periplasmic space.Membrane permeability Editorial overviewFranc PattusThe next review by Richard Reimer, Robert Fremeau, Elizabeth Bellocchio and Robert Edwards (pp 417–421) describes recent advances in our understanding of gluta-mate storage and release in synaptic vesicles owing to the identification of the long-sought after vesicular glutamate transporter, now dubbed VGLUT1, which was described previously as phosphate transporter. VGLUT1 is a new member of the large family of transporters from intracellu-lar membranes. These transporters represent around 30% of the ‘transportosome’ in the human genome.The importance of K+membrane permeability in living organisms is evident when looking at the long list of genes coding for K+channels subunits and at the large variety of subfamilies in terms of structure and function. In their review, Amanda Patel, Michel Lazdunski and Eric Honoré(pp422–427) focus on a novel class of mammalian K+chan-nels with four trans-membrane segments (4TMS) and two P domains (K+channels signature), focusing particularly on one of the four functional classes within this family—the lipid-sensitive mechano-gated K+channels.The unusual feature of these lipid-sensitive mechano-gated K+channels, TREK-1, -2 and TRAAK, is that channel activity is elicited by a mechanical pressure to the cell membrane but also by chemicals such as polyunsatu-rated fatty acids and anionic amphipaths, chemically unrelated compounds. A simple unifying theory suggest-ing a direct effect for the lipid bilayer and membrane curvature on the channel conformation—the bilayer cou-ple hypothesis—explains reasonably well how they are activated through apparently unrelated means. More than 40years ago, physicists working on surfactants and the polymorphism of the water/surfactants phases developed the simple concept of a direct relationship between the shape of the surfactant molecule and the curvature of the phase it forms in water (cone, cylinder, inverted cone). It is astonishing to see how well this concept can be used to interpret the activation of the lipid-sensitive mechano-gated K+channels.The identification of genes and the gene products mediating ion transport through membranes and involved in membrane permeability processes is advancing rapidly thanks to the combination of postgenomic tools with more classic but still efficient genetic, molecular and structural approaches.Cell compartimentalization which is especially well devel-oped in mammalian cells to optimise processes such as energy conversion, glycosylation reactions or degradation processes implies that membranes from intracellular organelles contain a large number of transporters to sup-port the necessary exchange of ion and molecules between these compartments and the cytoplasm of the cells. How these exchanges work and are regulated and how ion homeostasis is maintained through concerted action of transporters and channels from these internal membranes and from the cytoplasmic membranes are some of the key aspects of future investigation.One of the main challenges of the next years is to develop the necessary tools to study the concerted dynamics of these processes during the cell cycle, the response to stimuli and cell differentiation.388Membrane permeability。
电生理学
离子通道
(1)离子通道分类
钠通道 INa If 钙通道 电压门控钙通道:L,N,T,P,Q,R型; 配体调控性钙通道:IP3Rs,RyRs 钾通道 电压依赖性钾通道:Ikr, Iks, Ito, 等; 钙依赖性钾通道:BKCa, IKCa, SKCa等; 内向整流钾通道:KATP,KAch,IK1等; 氯通道 γ-氨基丁酸受体(GABA-R)
1963 SIR JOHN CAREW ECCLES, SIR ALAN LLOYD HODGKIN and SIR ANDREW FIELDING HUXLEY
Eccles
Hodgkin
Huxley
二、细胞的电活动 1.Resting potential
Intracellular Recording
一、发展简史: 1. Luigi Galvani--- 电生理学的奠基人,1786年 “凉台实验”,“无金属实验”。
Carlo Matteuci 1842年首次记录到肌肉的动作 电位,并用 “二次收缩实验”证明,动作电位引 起肌肉收缩。
L. Galvani (1737-1798)
animal electricity
A potential difference across the membranes of inactive cells, with the inside of the cell negative relative to the outside of the cell
K+ equilibrium
外面向外式
外部物质浓度可变
实验中膜内介质不能改变,微 管内需低钙以防囊泡形成
全细胞式
改变内部介质以分离电流
细胞电活动
(二)动作电位的产生机制
1、电化学驱动力:决定离子跨膜移动方向
静息电位- Na+受到很强的内向驱动力
锋电位---- K+受到很强的外向驱动力
•静息膜电位为﹣70mV 对Na+的驱动力:EM-ENa=﹣70mV-(+60mV)=﹣130mV 对K+的驱动力:EM-EK=﹣70mV-(﹣90mV)= +20mV
2、AP特征: ①全或无”性质:同一细胞上AP的大小不随刺激强度而改变。 ②可传播性:AP在同一细胞上的传播是不衰减的。不随传导距离而改变。 ③不融合:有不应期
3、意义:AP是细胞兴奋的标志, 传播信息, 触发细胞活动.
锋电位:pike potential是AP的标
升支 去极化+超射( –70 mV 迅速去极至+30mV 降支:复极化初期( +30迅速复极至接近–70 mV)
阈刺激或 大量的钠通道开放
阈上刺激
阈电位再生性循环 AP
2.电紧张电位 electrotonic potential: 膜电位随着跨膜电流的逐渐衰减而衰减的电位变化。
3,局部电位 local potential : 在电紧张电位基础上膜去极化,但此时外向钾电流大于内向钠电流,
膜电位又复极到静息电位水平的膜电位波动。 终板电位,感受器电位
当膜电位达到阈电位后,导致Na+通道开放与Na+内流之 间出现再生性循环。
(四) 动作电位的传播
AP在同一细胞上的传导::已兴奋部位和静息部位之间电荷移 动产生的局部电流.
AP在细胞间的传播:缝隙连接
三、 细胞兴奋后兴奋性的变化
Action Potential - Pegasus Web Server Home Pge动作电位-飞马Web服务器的主页
Not to study
• Donnans equilibrium • Osmolarity considerations
Action Potential
Changes in Ion Permeability allows inward Na flux and triggers an increased outward K flux through voltage gated ion channels Causes transient change in Membrane Potential The change in ion permeability is triggered by transient depolarization of the membrane
Conductance = g
• How many charges (ions) enters or leaves cell (inverse of resistance) • due to:
– number of channels/membrane area
• Highest density at axon hillock
Resting Membrane Potential
• Membrane potential at which neuron membrane is at rest, ie does not fire action potential • Written as Vr
Ionic Equilibrium Potential
Simplified Eion (at 37°C)
•Eion = 2.303 RT/zF log [ion]o/[ion]in • Ena = 61.54mV log [Na]o/[Na]I = 62 mV
循环系统-2010-2
Period of filling
Isovolumic relaxation
影响心输出量的因素
第二节 心肌的生物电现象和 生理特性
心肌细胞的生理特性 兴奋性 (Excitability) 自动节律性(Automaticity) 传导性 (Conductivity) 收缩性 (Contractility)
第四章
血液循环
(Circulation System)
朱毅
生理学与病理生理学系
增加前负荷,后负荷及心肌收缩力对P-V环
的影响
阻力最大,面积最小, SV最小
心室压小, 面积小, SV小
前负荷
后负荷
等容收缩期末P-V, 其斜率由心肌收缩力决定
心肌收缩力
Period of ejection
Isovolumic contraction
内向离子流,主要是Na+流
此期膜电位并不静息,而是负电位的绝对值自动逐 渐减少。当除极达-40mv左右时激活慢钙通道,产生 新的动作电位。
不同药物对起搏细胞firing rate作用
(ACh) (NE)
Sympathetic stimulation
Normal
Parasympathetic stimulation
快反应细胞
VM、AM、PF 快 大
缓慢、可分几期 快 Na+
-80~-95mv -60~-70mv
慢反应细胞
SAN、AVN 慢 小
缓慢、无明显分期 慢
Ca2+ -40~-70mv -30~-40mv
二.心肌生理特性 (Myocardial properties)
心肌具有自动节律性、兴奋性、传导性和 收缩性
– 4期不稳定,可自动缓慢去极化 (无静息期)
06.04 Membrane filters
Membrane filtersmolecular and ionic levels. Since the beginning of the 1970s, this technique has been adapted for the dairy industry. DefinitionsDefinitions of some frequently used expressions :Feed=the solution to be concentrated or fractionated. Flux=the rate of extraction of permeate measured inlitres per square meter of membrane surface areaper hour (l/m2/h)Membrane fouling=deposition and accumulation of feedcomponents on the membrane surface and/orwithin the pores of the membrane. Causes anirreversible flux decline during processing Permeate=the filtrate, the liquid passing through themembraneRetentate=the concentrate, the retained liquid Concentration factor=the volume reduction achieved byconcentration, i.e. the ratio of initial volume offeed to the final volume of concentrate/retentate Diafiltration=a design to obtain better purification. Water isadded to the feed during membrane filtrationwith the purpose to wash out low molecfular feedcomponents which will pass through themembranes, basically lactose and minerals. Membrane technologyIn the dairy industry, membrane technology is principally associated with •Reverse Osmosis (RO)– concentration of solutions by removal of water•Nanofiltration (NF)– concentration of organic components by removal of part of monovalent ions like sodium and chlorine (partial demineralisation)•Ultrafiltration (UF)– concentration of large and macro molecules, for example proteins •Microfiltration (MF)– removal of bacteria, separation of macro moleculesThe spectrum of application of membrane separation processes in the dairy industry is shown in Figure 6.4.1.All the above techniques feature pressure driven membrane filtration processes, in which the feed solution is forced through the membrane under pressure. The membranes are categorised by their NaCl retention (RO and NF) molecular weight cut-off (NF and UF), or nominal pore-size(MF). The cut-off is, supposedly the molecular weight of the smallest molecule that will not pass through the membrane. However, owing to various interactions, a membrane cannot be selected purely on the basis ofFig. 6.4.1 Spectrum of application of membrane separation processes in the dairy industry.The basic difference between conventional filtration and cross-flowmembrane filtration is illustrated in Figure 6.4.2.Several differences can be noted between conventional and membranefiltration.•Conventional filters are thick with open structures.Filter material is typically paper.Gravity is the main force affecting particle separation. Pressure may beapplied only to accelerate the process. The flow of feed is perpendicularto the filter medium, and filtration can be conducted in open systems.•Membrane filters are thin and of fairly controlled pore size.Filter material is polymers and ceramics, nowadays more rarely celluloseacetate.In membrane filtration, the use of a pressure difference across themembrane, a trans membrane pressure, TMP , is essential as driving forcefor separation and in cross-flow or tangential membrane filtration a flowdesign is followed. The feed solution runs parallel to the membrane surfaceFig. 6.4.2 Basic differences between conventional dead-end filtration and cross-flow membrane filtration.Feed flowand the permeate flows perpendicular to the membrane surface. The filtration must be carried out in a closed system.Principles of membrane separation The membrane separation techniques utilised in the dairy industry serve different purposes:RO–used for dehydration of whey, UF permeate and condensate.NF–used when partial desalination of whey, UF permeate orretentate is required.UF–typically used for concentration of milk proteins in milk and whey and for protein standardisation of milk intended for cheese, yoghurtand some other products. It is also used for clarification of fruit-and berry-juices.MF–basically used for reduction of bacteria in skim milk, whey and brine, but also for defatting whey intended for whey proteinconcentrate (WPC) and for protein fractionation.The general flow patterns of the various membrane separation systems are illustrated in Figure 6.4.3.Principles of membranefiltration.-3-2-11Reverse Osmosis (RO)MembraneNanofiltration (NF)Ultrafiltration (UF)Microfiltration (MF)Bacteria, fatProteinsLactoseMinerals (salts)WaterRetentateFiltration modulesThe filtration modules used may be of different configurations.Design Typical applicationPlate and frame UF , RO Tubular, based on polymers UF , RO Tubular, based on ceramics MF , UF Spiral-wound RO, NF , UF Hollow-fibre UF Plate and frame designThese systems consist of membranes sandwiched between membranesupport plates, which are arranged in stacks, similar to ordinary plate heatexchangers. The feed material is forced through very narrow channels thatmay be configured for parallel flow or as a combination of parallel and serialchannels. A typical design is shown in Figure 6.4.4.A module is usually divided into sections, in each of which the flow bet-ween pairs of membranes is in parallel. The sections are separated by aspecial membrane support plate in which one hole is closed with a stopdisc to reverse the direction of flow, giving serial flow between successivesections. Modules are available in various sizes.Membrane material: typical polymers.Tubular design – polymersThe system made by Paterson and Candy International Ltd, PCI, is anceramic membranes is steadily gainingThe filter element (Figure 6.4.6) is a ceramic filterThe thin walls of the channels are made of fine-grainedceramic and constitute the membrane. The support material is coarse-The filter elements (1, 7, 19 or 37 in6.4.7 shows a module with 19 filterelements, one of which is exposed tothe left of the module. For industrialpurposes, two modules are puttogether in series, forming a filterloop together with one retentatecirculation pump and one permeate circulation pump (Figure 6.4.10).Depending on the required Fig. 6.4.4 Example of a plate and frame system (DDS) for UF .collectorFig. 6.4.10 An industrial membrane filter loop consists of:–two filter modules connected in series –one retentate circulation pump –one permeate circulation pumpFig 6.4.9 Pressure drop at the Uniform Transmembrane Pressure system.Fig 6.4.8 Pressure drop during conventionalcross-flow microfiltration.capacity, a number of filter loops can be installed in parallel.The feed is pumped into the modules from below at a high flow rate. Thehigh flow rate causes a high pressure drop along the membrane elementswhich leads to an uneven transmembrane pressure (TMP), the TMP beinghigher at the inlet than at the outlet. The very high TMP at the inlet quicklycauses clogging of the membrane. This phenomenon is illustrated in Figure6.4.8, which shows conventional cross-flow microfiltration. Experienceshows that a low transmembrane pressure gives much better performance,but in conventional cross-flow microfiltration, a low transmembranepressure occurs only at the outlet, i.e. on a very small part of the membrane area.A unique Uniform Transmembrane Pressure (UTP) system has beenintroduced to achieve optimum conditions on the entire area. The patented system, illustrated in Figure 6.4.9, involves high-velocity permeatecirculation concurrently with the retentate creating a pressure drop on thepermeate side which is equal to the pressure drop on the retentate side.This gives a uniform TMP over the whole of the membrane area, withoptimum utilisation of the membrane.The latter system is possible because the space between the elementsinside the module, i.e. on the permeate side, is normally empty, but in theUTP version, it is filled with plastic grains. The pressure drop on thepermeate side is regulated by the permeate pump and is constant duringoperation of the plant.Today membrane elements of special design which have this so calledUTP system built-in in their structure are available. When using this type ofmembranes there is no need for a circulation on the permeate side. TheseSpiral-wound designAs the spiral-wound design differs from the othermembrane filtration designs used in the dairyindustry, it calls for a somewhat more detailedexplanation.A spiral-wound element contains one or morelayers of membrane separated by a porousthe permeate channel spacer passing through the membrane to flow freely. Thetwo layers of membrane with the permeate channel Bar Bar Pressure profilesBar BarPressure profiles spiral-wound filter design.elements to prevent the velocity of treated fluid from causing the layers to slip.Several elements – normally three – can be connected in series inside the same stainless steel tube as shown in Figure 6.4.13.Membrane and permeate spacer material: polymer.Hollow-fibre designHollow-fibre modules are cartridges which contain bundles of 45 to over 3000 hollow-fibre elements per cartridge. The fibres are oriented in parallel;all are potted in a resin at their ends and enclosed in the permeatecollecting tube of epoxy.Circulation of retentate Backflush with permeate Cleaning solution ProductFig. 6.4.14 UF cartridge during filtration(A), backflushing (B) and cleaning (C).Fig.6.4.13 Spiral-wound module assembly. Either or both of the pairs of connecting branches (X and Y) can be used for stackable housing, specially used in UF con-cepts.The membrane has an inner diameter ranging from 0,5 to 2,7 mm, and the active membrane surface is on the inside of the hollow fibre. Theoutside of the hollow-fibre wall, unlike the inner wall, has a rough structure and acts as a supporting structure for the membrane. The feed stream flows through the inside of these fibres, and the permeate is collected outside and removed at the top of the tube.A special feature of this design is its backflushing capability, which is utilised in cleaning and with permeate recirculated through the outer per-meate connection to remove product deposits on the membrane surface.Various modes of operation of a hollow-fibre module are illustrated in Figure6.4.14.Membrane material: polymers.Separation limits for membranes The separation limit for a membrane is determined by the lowest molecular weight that can be separated. Themembrane can have a definite or a diffuse separation limit,as illustrated in Figure 6.4.15 for two UF membranes. The same phenomena occur in other types of membrane separators, but the slope of the curves may be different.Membranes with a definite separation limit separateeverything with a definitely lower molecular weight, whilemembranes with a diffuse limit let some material with ahigher molecular weight through and stop some with a lower molecular weight.The separation accuracy of a membrane is determinedby pore size and pore size distribution. Because it is not possible to carry out an exact fractionation according to molecular mass or molecular diameter, the cutoff is more or less diffuse.The definition that the molecular weight determines the separation limit should be taken with some reservations, as the shape of the separated particles also has an influence. A spherical particle is easier to separate than a chain-shaped particle. In addition comes the build-up of a "secondarymembrane" by macromolecules, e.g. proteins, which may constitute the membrane that really determines the molecular cutoff value.Material transport through the membraneSeparation capacity depends on a number of factors:•Membrane resistance, which is characteristic for each membrane and is determined by– the thickness of the membrane– the surface porosity– the pore diameter•Transport resistance, i.e. the concentration polarisation and fouling effects are phenomenon which occurs at the surface or in the porous structure of the membranes as filtration proceeds.The formation of a layer which increase the resistance can be explained as follows:•Large molecules (i.e. protein and fat) are transported by convection to the membrane at right angles to the direction of flow. Due to theretention the concentration of particles will increase at the membrane surface.•This concentration gradient produces a back diffusion in the opposite direction, back to the bulk.•Parallel to the membrane, the proteins present in the layer close to the membrane surface move at velocities which vary according to theincrease in axial flow rate.0R e j e c t i o n C o e f f i c i e n tMolecular weight Fig. 6.4.15 Typical rejection characteris-tics of ultrafiltration membranes showing ideal, sharp and diffuse molecular weight cutoffs.•The fouling effect is not uniformly distributed along the membrane, especially when the pressure drop gives different transmembranepressures (TMP) along the membrane surface. The upstream end of the membrane is therefore clogged first. The fouling graduallyspreads over the whole surface, reducing capacity and eventuallymaking it necessary to stop and clean the plant.•The main effect of fouling is that the removal of permeate decreases as filtration proceeds.•The fouling effect can be reduced in certain concepts by using backflush, reverse flow or UTP (possible when ceramic membranes are used).Pressure conditionsPressure is the driving force of filtration, and an important distinction must be made between:1The hydraulic pressure drop along the module P = P1- P2.The higher the velocity through the module the higher the value of P. A higher velocity results in a higher shear at the membrane surface and a lower polarisation effect. However, there are constraints such as theresistance to pressure of the membrane and the price of pumps capable of delivering both high flows and high pressure.2The transmembrane pressure (TMP) is the pressure drop between the retentate and the permeate sides of the membrane at a particular point along the membrane. The main criterion of the efficiency of a membrane system is expressed as the flux – the flow per membranes area andhour, l/m2/h, and is a function of TMP.The TMP, i.e. the force which pushes the permeate through the membrane, is greatest at the inlet and lowest at the discharge end of the module. Since the decrease in TMP is linear, an average TMP is given by:Fig. 6.4.16Hydraulic (A) and transmembrane (B) pressure drops over a membranePP31P PP1A B0barP1= inlet pressure feedP2= outlet pressure concentrate P3= outlet pressure permeate Pressure profilesThe hydraulic pressure drop over the membrane (A) and the transmembrane pressure profile (B) are illustrated in Figure 6.4.16.Principles of plant designsThe operation of membrane filtration plants dependsbasically on the pressure generated by the pumps used.The following guides should be taken into consideration:1The capacity of the pump(s) should match the requiredvary widely according to module design and size.2The pump(s) should be insensitive to changes in theviscosity of the processed stream up to the viscosity3The pump(s) must satisfy the sanitary standards fordairy equipment.Pumps of several types are used, including centrifugalpumps and positive displacement pumps. Sanitary cen-trifugal pumps are normally used as feed and circulationpumps, but sanitary positive displacement pumps areoccasionally used as high-pressure feed and circulationpumps for high-viscosity liquids, e.g. in the final stages ofultrafiltration of acidified milk.Membrane separation plants can be used for bothbatch and continuous production. The feed solution mustnot contain coarse particles , which can damage the verythin filtration layer/active layer. A fine-meshed strainer istherefore often integrated into the feed system.Batch productionPlants for batch production (Figure 6.4.17) are used mainlyfor filtration of small volumes of product, for example inlaboratories and experimental plants. A certain amount ofthe product to be treated is kept in a buffer tank. Theproduct is circulated through the membrane separator untilthe required concentration is obtained.Continuous productionSchematic designs of the membrane filtration plants re-ferred to are collected in Figures 6.4.18. and 6.4.19. Theplants illustrated in Figure 6.4.18 represent spiral-woundconcepts for RO, NF and UF applications, with polymermembranes of different pore sizes, while Figure 6.4.19shows a MF plant with ceramic membranes.As the RO membranes are much tighter than those of the two other systems, a higher inlet pressure is required for production. This is main-Fig. 6.4.17 Batch membrane filtration plant Feed product Concentration loop Permeate Cooling medium 1Product tank 2Feed pump 3Circulation pump 4Strainer 5Membrane module 6CoolerRO concept NF concept UF concept Fig. 6.4.18 Design principles for different filter loops.1Membrane 2Cooler3StrainerRetentatePermeate Fig. 6.4.191MF membrane cartridge2Circulation pump for retentate Fig. 6.4.20tained by three sanitary centrifugal feed pumps in series and one sanitary centrifugal circulation pump.The other two filtration plants, NF and UF , have more open membranes and can therefore manage with two feed pumps and one feed pump respectively.As was mentioned earlier, the MF concept is based on two filter modules operated in series in a filter loop system which also contains one centrifugal pump for circulation of the retentate and one for circulation of the permeate.The feed solution may be supplied from a separation plant with a system for constant pressure at the outlet, or from a balance tank equipped with a pump and a system for capacity regulation.Processing temperature in membranefiltration applicationsIn most cases, the processing temperature is about 50 °C for dairy applications. Filtration plants are normally supplemented with a simple cooling system integrated into the internal circulation loop to compensate for the slight rise in temperature that occurs during operation and to maintain a constant processing temperature.。
碱性膜燃料电池阴极Co-N-C催化剂层的性能优化
第54卷 第4期 2021年4月天津大学学报(自然科学与工程技术版)Journal of Tianjin University (Science and Technology )V ol. 54 No. 4Apr. 2021收稿日期:2020-06-28;修回日期:2020-09-15.作者简介:尹 燕(1974— ),女,博士,教授,**************.cn. 通信作者:张俊锋,***************.cn .基金项目:天津市自然科学基金资助项目(18JCQNJC07100,17JCZDJC31000).Supported by the Natural Science Foundation of Tianjin ,China (No.18JCQNJC07100,No.17JCZDJC31000).DOI:10.11784/tdxbz202006069碱性膜燃料电池阴极Co -N -C 催化剂层的性能优化尹 燕,裴亚彪,祝伟康,张俊锋(天津大学内燃机燃烧学国家重点实验室,天津 300350)摘 要:近年来,阴离子交换膜性能的提升使碱性膜燃料电池(AMFC )的研究成为热点.与质子交换膜燃料电池(PEMFC )相比,其主要特点之一就是可以使用非贵金属催化剂替代商业Pt/C ,从而避免非贵金属在酸性中的不稳定性.膜电极是燃料电池的核心部件,制约燃料电池的性能.催化层作为膜电极的主要部件,由催化剂和离聚物组成.离聚物质量分数影响催化层孔的尺寸和分布,从而影响电化学反应速率和燃料电池反应中的氧扩散和水传输.同时,催化层与气体扩散层接触的紧密程度也影响了接触电阻.因此,对催化层微观结构的调控决定着燃料电池发电性能.目前,关于AMFC 的催化层研究以贵金属Pt/C 催化剂为主,对于非贵金属催化层研究相对较少,制约了其在碱性膜燃料电池中的应用.本文使用实验室自制的Co-N-C 催化剂和商业FAA-3离聚物制备了阴极催化层,探究了Co-N-C 催化层中离聚物的质量分数对催化层结构的影响,通过研究催化剂墨水的组分和配比,发现当离聚物质量分数为40%时燃料电池性能最高达到139.7mW/cm 2,与使用Pt/C 催化剂的燃料电池性能相近. 关键词:碱性膜燃料电池;膜电极;非贵金属催化层;离聚物质量分数中图分类号:TK9 文献标志码:A 文章编号:0493-2137(2021)04-0374-05Optimization of a Cathode Co -N -C Catalyst Layer foran Alkaline Membrane Fuel CellYin Yan ,Pei Yabiao ,Zhu Weikang ,Zhang Junfeng(State Key Laboratory of Engines ,Tianjin University ,Tianjin 300350,China )Abstract :Recently, with the improvement in the performance of anion exchange membranes ,the research on alka-line membrane fuel cells (AMFCs) has become active. Compared with the proton-exchang e membrane fuel cell (PEMFC ),one of the main advantages of the AMFC is that non-noble metal catalysts can be used to replace com-mercial Pt/C ,thereby avoiding the instability of non-noble metals in an acid environment. A membrane electrode assembly (MEA) is the core component of fuel cells ,and it restricts the fuel cell performance. A catalyst layer com-posed of a catalyst and an ionomer is the main component of the MEA. The ionomer content determines the pore size and distribution ,thereby affecting the electrochemical reaction rate ,oxygen diffusion ,and water transport. More-over ,the contact between the catalyst layer and gas diffusion layer also influences the contact resistance. Therefore ,tuning the microstructure of the catalyst layer is important to the fuel cell performance. At present ,most researchers focus on the noble metal Pt/C catalyst layer ,while the works on non-noble-metal catalyst layers are few ,limiting their application in AMFCs. In this study ,a laboratory-made non-noble metal catalyst Co-N-C and a commercial FAA-3 ionomer were used to fabricate a cathode catalyst layer of MEA ,and the influence of the ionomer content in the Co-N-C catalyst layer structure was explored. The maximum performance of the fuel cell was found to be 139.7mW/cm 2 with the ionomer content of 40%,which was close to the performance of the fuel cell with a Pt/C catalyst layer.Keywords :alkaline membrane fuel cell ;membrane electrode ;non-noble metal catalyst layer ;ionomer content新世纪以来,社会发展迅速,能源需求急剧增加,环境污染日益严重.为了改善环境问题,可再生2021年4月尹 燕等:碱性膜燃料电池阴极Co-N-C催化剂层的性能优化 ·375·能源的使用受到越来越多人的重视.燃料电池(fuel cell,FC)作为氢能的一种利用方式,能够将燃料的化学能高效、清洁地转变为电能.由于不经历燃烧过程,不受卡诺循环的限制,故具有很高的转换效率[1-3].与质子交换膜燃料电池(proton exchange membrane fuel cell,PEMFC)比较,碱性膜燃料电池(alkaline membrane fuel cell,AMFC)具有氧还原动力学反应较快(碱性环境),可以使用非贵金属催化剂,燃料交叉率低、工作温度低等优点,近年来受到越来越多的科研工作者的关注[4-6].膜电极作为燃料电池的核心部件,由离子交换膜、阴阳极催化层和气体扩散层组成.膜的离子电导率决定着离子的传输速率,进而影响整体的化学反应速率.三相界面,也就是催化层中的催化剂、离聚物和反应气体交界处,是电化学反应的主要场所,决定着电化学反应速率的快慢,直接影响燃料电池的性能.为了降低燃料电池的制造成本,加快其商业化进程,近年来,大多科研工作者都将精力集中在膜电极中的膜和催化剂,并取得了一定进展(电池功率密度超过1W/cm2)[7-10].然而,对于催化层结构,尤其是非贵金属催化剂制备的催化层,依然需要进一步研究.并且,近年来大多数关于催化层结构的研究都是围绕贵金属Pt/C催化剂所展开[4,11-13],对非贵金属催化剂层的研究有待进一步深入.研究表明,离聚物是催化层内离子和气体扩散的主要通道,对电化学反应过程有重要的影响,研究表明,当离聚物质量分数为25%时(对Pt/C催化剂而言)燃料电池性能达到最 优[14].离聚物质量分数较低时催化剂不能完全被离聚物覆盖,降低了催化剂的利用率;离聚物质量分数较高时导致大量离聚物和催化剂团聚,减少三相界面,亦会阻塞孔隙,增大传质损失[15].此外,溶剂类型也对催化层的微观结构具有重要影响[4,16-18],通过比较溶剂法和胶体法制备的催化层,发现胶体法制备的膜电极催化层有更多的连续不断的离子传输通道以及三相界面,这将会加快电化学反应速率,提升燃料电池性能.然而关于非贵金属催化层的研究目前还比较少,阻碍了碱性膜燃料电池的商业化发展和应用.本文以自制的Co-N-C作为阴极催化剂,主要研究了离聚物质量分数和膜电极制备方法(溶液法和胶体法)对其催化层结构及性能的影响.1 实 验1.1 实验材料本实验使用的材料包括六水合硝酸钴(阿拉丁,99.9%-Co),聚乙烯吡咯烷酮(PVP,麦克林),炭黑(XC-72,Vulcan),超纯水,甲醇(安耐吉,99%),2-甲基咪唑(Merck,99%),高氯酸(HClO4,阿拉丁,85%),商业碱性膜(FAA-3-20/50,FuMA-Tech)和离聚物(FAA-3SOLUT-10,FuMA-Tech,质量分数为10%),60%Pt/C(Johnson Matthey,UK)催化剂,自制非贵金属Co-N-C催化剂[1],异丙醇(IPA,安耐吉,99%)和四氢呋喃(THF,安耐吉,99%).1.2 Co-N-C催化剂的合成将1.164g 六水合硝酸钴(Co(NO3)26H2O)+0.6g PVP+100mg炭黑溶解于40mL甲醇中,并将2.46g 2-甲基咪唑溶解于另一40mL甲醇中,将两种混合物分别超声分散5min.然后将两种溶液在400r/min、4℃下搅拌40min并在室温下静置72h以生长沸石咪唑酯骨架结构材料(ZIF)-炭黑(CB).ZIF 经离心干燥后,在Ar气氛下于700 ℃热解2h,得到ZIF衍生催化剂.最后,在室温下用0.1mol/L HClO4洗涤催化剂,继而用离心分离法从酸性溶液中回收催化剂,并在60℃下干燥24h,即得到催化剂样品(ZIF-CB-700)[1].1.3 膜电极制备及单电池测试本实验采用将催化剂墨水喷涂在膜上(catalyst coated membrane,CCM)的方法制备膜电极,即取一定量的催化剂于干净小瓶中,加少量去离子水使催化剂充分润湿,然后加入分散溶剂,在冰水混浴中超声10min,接着加入离聚物溶液并超声30min即制备好催化剂墨水.用移液枪量取一定量催化剂墨水于喷枪中并将其喷涂在膜(有效面积为4cm2)上,控制Pt/C 催化剂中Pt载量为0.4mg/cm2以及非贵金属Co-N-C 催化剂载量为2mg/cm2.将制备好的膜电极在室温下浸入1mol/L KOH溶液中24h,将膜中的Br-置换成OH-.然后用4N·m的力矩将膜电极组装到单电池中并连接到燃料电池测试台(Greenlight G60,Canada)进行测试.氢气和氧气流量分别为100mL/min和200mL/min,测试温度为40℃,相对湿度为100%.1.4 催化层结构分析通过扫描电子显微镜(Hitachi,S-4800)观察并分析了催化层断面结构.将制备好的膜电极浸泡在液氮中30s左右,然后淬断并固定在样品台上进行观察,测试电压为5kV.2 结果和讨论2.1 离聚物质量分数的影响为了研究离聚物对非贵金属Co-N-C催化剂的·376·天津大学学报(自然科学与工程技术版)第54卷 第4期影响,制备了5种不同离聚物质量分数(从30%逐渐变化至50%)的阴极催化层,阳极使用Pt/C催化剂(离聚物质量分数25%),实验结果如图1所示.当阴极离聚物质量分数从30%增加到40%时,燃料电池的性能不断增加,而随着离聚物质量分数继续增加到50%时,燃料电池性能逐渐降低.当离聚物质量分数图1离聚物质量分数对燃料电池性能的影响 Fig.1Influence of ionomer content on fuel cell perform-ance 为40%时,燃料电池性能最好,最大功率密度达到87.5mW/cm2.为了更清晰地观察离聚物质量分数对燃料电池性能的影响,通过扫描电子显微镜实验对催化层断面进行分析,如图2所示.当离聚物质量分数较少(占比为35%),催化剂被离聚物包裹的较少(较亮区域),减少了三相界面面积,导致有效电化学反应面积降低,从而降低燃料电池性能.图2(c)和(d)催化层中离聚物质量分数分别为45%和50%,可以看出离聚物质量分数较多(较亮区域),导致大量离聚物和催化剂团聚,从而降低催化剂的利用率,减少了三相界面面积,同时离聚物过多亦会阻塞催化层中的孔隙,这可能导致传质损失,因此燃料电池性能较低.当催化层中离聚物质量分数为40%时(图2(b)),离聚物分布较为均匀,团聚现象不明显,增大了三相界面面积,有效地利用了催化剂,从而获得较高的燃料电池性能.(a)离聚物质量分数为35%(b)离聚物质量分数为40%(c)离聚物质量分数为45%(d)离聚物质量分数为50%图2不同离聚物质量分数Co-N-C催化剂层扫描电子显微镜图Fig.2Scanning electron microscopy images of Co-N-C catalyst layer with different ionomer contents2.2 不同膜厚及溶剂的影响为了进一步提升燃料电池的性能,继续探讨了膜厚度和分散溶剂的影响,测试结果如图3所示(阳极Pt/C催化剂中Pt载量:0.4mg/cm2,阴极Co-N-C载量:2mg/cm2).当使用异丙醇做分散溶剂,将膜厚从50µm降低至20µm时,燃料电池性能从87.5mW/cm2提升至118.6mW/cm2,这得益于膜厚降低,膜的离子电导率增加,离子传输路径缩短,从而提高了燃料电池性能.随后,使用20µm厚的阴离子交换膜,相对于异丙醇(溶液法制备膜电极)溶剂,使用四氢呋喃(胶体法制备膜电极)做溶剂时,燃料电池性能进一步提升到139.7mW/cm2.为了深入研究溶剂对催化层结构的影响,进行了扫描电子显微镜(图4)实验,对膜电极催化层结构进行分析.从图4可以看出,使用异丙醇制备的膜电极催化层孔径分布不均,有较大的孔隙结构(>2µm)(图4(a)),而使用四氢呋喃做溶剂制备的膜电极催化层有较均匀的孔隙分布(图4(c)),均匀分布的孔隙结构有利于气体扩散,较大的孔径将会导致催化层疏松,这将增大电荷转移电阻.2021年4月尹 燕等:碱性膜燃料电池阴极Co-N-C催化剂层的性能优化 ·377·图3膜厚及溶剂对燃料电池性能的影响Fig.3Influence of membrane thickness and solvent on fuel cell performance(a)异丙醇(b)图(a)中红色方框部分放大(c)四氢呋喃(d)图(c)中黄色方框部分放大图4不同溶剂的Co-N-C催化层扫描电子显微镜图Fig.4Scanning electron microscopy images of Co-N-C catalyst layer for different solvents 2.3 贵金属与非贵金属催化剂的比较将优化的Co-N-C催化层的结果与使用贵金属Pt/C催化剂层进行比较,如图5所示.膜电极阴、阳极使用Pt/C催化剂,Pt载量都为0.4mg/cm2的燃料电池性能达到了152.3mW/cm2,而将阴极Pt/C催化剂替换为Co-N-C(载量为2mg/cm2)时,最大功率密度达到了139.7mW/cm2.从图5可以看出,阴极催化剂使用非Pt/C时,燃料电池性能并无明显降低,而且电池在100mA/cm2下,长时间运行10h后,电压无明显下降(图6).这将大幅度降低燃料电池的制造成本,有利于促进碱性膜燃料电池商业化.图5阴极催化剂为Pt/C和Co-N-C的燃料电池性能的比较Fig.5Comparison of fuel cell performance for the cath-ode prepared with Pt/C and Co-N-C图6在100 mA/cm2下阴极催化剂为Co-N-C的燃料电池的耐久性测试Fig.6Durability test of fuel cell with Co-N-C cathode at 100mA/cm23 结 语为了探究Co-N-C催化层结构与其燃料电池性能之间的关系,本研究探讨了离聚物质量分数、溶剂等因素的影响.首先,制备了离聚物质量分数为30%~50%的催化层,实验结果表明,当离聚物质量分数为40%时性能达到最高,当离聚物质量分数较低时,催化剂被离聚物包裹的较少,减少了三相界面区域,催化剂利用率降低;离聚物质量分数较高时,·378·天津大学学报(自然科学与工程技术版)第54卷 第4期大量离聚物和催化剂团聚,也减少了三相界面,同时离聚物过多亦会阻塞催化层中的孔隙,增加传质损失,影响了燃料电池性能.其次,选取了两种不同的溶剂,发现使用四氢呋喃(胶体法)制备的膜电极催化层孔径分布较为均匀,进一步提高了燃料电池性能.最后,将自行研发的使用非贵金属催化剂制备的膜电极与使用Pt/C催化剂的膜电极进行比较,发现当阴极催化层使用Co-N-C时燃料电池性能与传统Pt/C膜电极性能非常接近,说明非贵金属催化剂有望完全替代Pt/C应用在碱性膜燃料电池的阴极.参考文献:[1]Zhang Junfeng,Zhu Weikang,Pei Yabiao,et al. 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Membrane Potential and Firing Rate in Cat Primary Visual CortexMatteo Carandini1,2,3and David Ferster31Institute for Neuroinformatics,Swiss Federal Institute of Technology and University of Zurich,CH-8057Zurich, Switzerland,2Howard Hughes Medical Institute and Center for Neural Science,New York University,New York10003, and3Department of Neurobiology and Physiology,Northwestern University,Evanston,Illinois60208We have investigated the relationship between membrane po-tential andfiring rate in cat visual cortex and found that the spike threshold contributes substantially to the sharpness of orientation tuning.The half-width at half-height of the tuning of the spike responses was23Ϯ8°,compared with38Ϯ15°for the membrane potential responses.Direction selectivity was also greater in spike responses(direction index,0.61Ϯ0.35) than in membrane potential responses(0.28Ϯ0.21). Threshold also increased the distinction between simple and complex cells,which is commonly based on the linearity of the spike responses to drifting sinusoidal gratings.In many simple cells,such stimuli evoked substantial elevations in the mean potential,which are nonlinear.Being subthreshold,these ele-vations would be hard to detect in thefiring rate responses. Moreover,just as simple cells displayed various degrees of nonlinearity,complex cells displayed various degrees of linearity.Wefitted thefiring rates with a classic rectification model in whichfiring rate is zero at potentials below a threshold and grows linearly with the potential above threshold.When themodel was applied to a low-pass-filtered version of the mem-brane potential(with spikes removed),the estimated values ofthreshold(Ϫ54.4Ϯ 1.4mV)and linear gain(7.2Ϯ0.6spikes⅐secϪ1⅐mVϪ1)were similar across the population.The predictedfiring rates matched the observedfiring rates well andaccounted for the sharpening of orientation tuning of the spikeresponses relative to that of the membrane potential.As it was for stimulus orientation,threshold was also inde-pendent of stimulus contrast.The rectification model ac-counted for the dependence of spike responses on contrastand,because of a stimulus-induced tonic hyperpolarization,forthe response adaptation induced by prolonged stimulation.Because gain and threshold are unaffected by visual stimulationand by adaptation,we suggest that they are constant under allconditions.Key words:threshold;summation;iceberg;tuning;linearity;orientation;contrast;adaptation;simple cells;complex cellsA mechanism that contributes to the remarkable selectivity of cells in the visual cortex is the action potential threshold.Because neurons in the visual cortex are mostly quiet in the absence of visual stimulation,their average membrane potential at rest must lie somewhat belowfiring threshold.In principle,therefore,the tuning of thefiring responses of visual cortical neurons could represent the tip of an iceberg:just as icebergs are wider below the surface of the water than above it,the tuning of the synaptic inputs to a cell could be broader below threshold than above it.In the domain of orientation selectivity,a comparison of tuning curves measured from the membrane potential(Nelson et al., 1994;Pei et al.,1994;Volgushev et al.,1995,1996;Ferster et al., 1996;Chung and Ferster,1998)and from thefiring rate(Camp-bell et al.,1968;Rose and Blakemore,1974a;Gizzi et al.,1990) suggests that threshold does contribute to the sharpness of tuning. Is this contribution substantial?This question is relevant to the intense debate surrounding the mechanism of orientation selec-tivity(Reid and Alonso,1996;Vidyasagar et al.,1996;Sompolin-sky and Shapley,1997):if the sharpening provided by the thresh-old were prominent,then cells would not need to receive synaptic inputs that are sharply tuned.Another major theme in the current research on the primary visual cortex centers on simple cells and regards the degree to which the responses of these cells are linear.Linearity was im-plicit in the original descriptions of simple cells(Hubel and Wiesel,1962)and was investigated by Movshon et al.(1978a)and by a multitude of subsequent studies(for review,see Carandini et al.,1999).Most of these measurements were performed on the spike responses and were thus limited by the intrinsic nonlinearity of threshold.Intracellular measurements of membrane potential are not subject to this limit but have so far yielded mixed results. Jagadeesh et al.(1993,1997)argued in favor of the linear model, but Volgushev et al.(1996)found indirect evidence for nonlin-earity,and recent measurements of the mean potential responses to gratings(Carandini and Ferster,1997)suggest that simple cells can be quite nonlinear.Overall,a number of questions remain open,including(1)the degree to which simple cells are nonlinear, (2)the effects of this nonlinearity on their tuning for orientation, and(3)the degree to which complex cells and simple cells differ (and can be distinguished by)their linearity.In the experiments presented in this paper,we have examined the relationship between membrane potential andfiring rate in neurons of the cat visual cortex.We have found that the iceberg effect does contribute significantly to orientation and direction selectivity:the orientation tuning of cortical cells as measured from their action potentials is considerably sharper than theReceived April9,1999;revised Aug.23,1999;accepted Oct.18,1999.This work was supported by National Institutes of Health Grant EY04726toD.F.M.C.was partly supported by a Howard Hughes Medical Institute investiga-torship to J.A.Movshon.We thank Dario Ringach and Todd Troyer for advice andencouragement.Correspondence should be addressed to Matteo Carandini,Institute of Neuroin-formatics,ETH/University of Zurich,Winterthurerstrasse190,CH-8057Zu¨rich,Switzerland.E-mail:matteo@ini.unizh.ch.Copyright©1999Society for Neuroscience0270-6474/99/200470-15$15.00/0The Journal of Neuroscience,January1,2000,20(1):470–484orientation tuning measured directly from the membrane potential.We have also investigated the linearity of the membrane po-tential responses and found that threshold also increased the distinction between simple and complex cells.This distinction is commonly based on the linearity of the spike responses to drifting sinusoidal gratings.In many simple cells,such stimuli evoked substantial elevations in the mean potential,which are nonlinear. Being subthreshold,these elevations would be hard to detect in thefiring rate responses.Moreover,just as simple cells displayed various degrees of nonlinearity,complex cells displayed various degrees of linearity.Afinal issue that we have addressed concerns the relationship between membrane potential andfiring rate.We have tested what is perhaps the simplest model for this relationship:the rectifica-tion model(Granit et al.,1963).This model has been used explicitly or implicitly in much of the literature on the response of visual cortical neurons(Movshon et al.,1978a;Ahmed et al., 1998;Carandini et al.,1999)and postulates that thefiring rate is zero below the spike threshold and grows linearly above thresh-old.We found that the relationship between membrane potential andfiring rate is well described by the rectification model.The model cannot of course predict the timing of individual spikes but accurately predicts the slower variations infiring rate in response to visual stimuli.A preliminary version of the results has been presented in abstract form(Carandini and Ferster,1998).MATERIALS AND METHODSDetails of most procedures have been described previously(Ferster and Jagadeesh,1992;Carandini and Ferster,1997;Jagadeesh et al.,1997). For those procedures,we give only a summary description here. Experimental preparation.Young adult cats were anesthetized with intravenous sodium thiopental and placed in a stereotaxic headholder. Paralytic agents(gallamine or pancuronium)were administered to min-imize motion of the eyes,and the animals were artificially respirated. Phenylephrine hydrochloride and atropine sulfate were applied to the eyes to retract the nictitating membranes,dilate the pupils,and paralyze accommodation.Contact lenses with artificial pupils(4-mm-diameter) were inserted.Visual stimulation.Visual stimuli consisted of monocularly presented drifting sine-wave gratings displayed on a Tektronix(Wilsonville,OR) 608oscilloscope screen using a Picasso stimulus generator(Innisfree, Cambridge,MA).The peak contrast used was64%,and the mean luminance(kept constant throughout the experiments)was20cd/m2. Optimal spatial frequency was determined from computer-generated spatial frequency tuning curves.Grating size,position,and temporal frequency were adjusted to be optimal,usually by hand.To generate orientation tuning curves,stimuli of12different orienta-tions(0–330°)were presented in random order,4sec for each orienta-tion.The contrast of the gratings was usually47%,and the block of stimuli included an additional4sec blank screen presentation.This block of13stimuli was repeated two tofive times for each cell,with a different randomized order each time.To generate contrast–response curves,stimulus blocks consisted of seven optimally oriented stimuli with contrasts logarithmically spaced between1and64%,which were randomly presented.Test stimuli were4 sec long and were preceded by4sec adaptation stimuli(20sec before the first test stimulus),as previously described(Carandini and Ferster,1997). Intracellular recording.Whole-cell patch recordings in the current-clamp mode were obtained from neurons of area17of the visual cortex using the technique developed for brain slices by Blanton et al.(1989). Electrodes werefilled with a Kϩ-gluconate solution including Ca2ϩbuffers,pH buffers,and cyclic nucleotides.Junction potentials were measured to be10mV.This value was added to the membrane potentials reported in this study.Input resistance ranged typically between70and 250M⍀.Membrane potentials were low-pass-filtered and digitized at4 kHz,and the timing of spikes was logged with250sec accuracy. Response measures.To obtain tuning curves for the membrane poten-tial and spike train responses we considered two response measures,the mean and the modulation.The mean response was the average over the 4sec stimulus presentation,whereas the modulation was the peak-to-peak amplitude of the best-fitting sinusoid at the stimulus frequency(obtained by fast Fourier transform).For this analysis,individual spikes were treated as Dirac␦functions.Tuning curves.The orientation tuning of the responses wasfitted with a descriptive function.This function is the sum of two Gaussians and is defined on the circle.The two Gaussians are forced to peak180°apart and to have the same width:f͑O͒ϭR0ϩR p eϪ͗OϪO p͘2/͑22͒ϩR n eϪ͗OϪO pϩ180͘2/͑22͒.(1)In the above expression,O is the stimulus orientation(between0and 360°),and the angle brackets indicate angular values expressed between Ϫ180and180°.The function hasfive parameters:the preferred orien-tation,O p;the tuning width,;the base response,R0;and the increment in response at the preferred and null orientations,R p and R n,which correspond to the heights of the two Gaussians.This function assigns the same tuning width(but not necessarily the same amplitude)to the responses to opposite directions of motion.Consistent with previous results on the tuning of thefiring rate responses(Campbell et al.,1968), we found that this constraint was appropriate in all of our data sets. To allow us to report a single preferred orientation and tuning width for each signal,membrane potential andfiring rate,the mean and the modulation for each signal werefitted together.In particular,although the base response and the heights of the two Gaussians were allowed to differ for mean and modulation,an additional constraint was applied such that thefits to these measures had the same preferred orientation,O p, and tuning width,.This constraint did not noticeably worsen thefits and would not affect the comparisons between the tunings of the mem-brane potential responses and thefiring rate responses,which werefitted independently from one another.Measures of response tuning.From the parameters of Equation1,it is easy to obtain some widely used measures of response tuning,namely the direction index and the orientation tuning half-width.The direction index is a common measure of direction selectivity (Schiller et al.,1976;Orban et al.,1981;Reid et al.,1987;Gizzi et al., 1990).We define this index as do Reid et al.(1987),i.e.,as the difference in the responses obtained with stimuli of preferred and opposite direc-tions of motion,divided by the sum of those responses.In terms of the parameters of the model,the direction index is then(PϪN)/(PϩN), where PϭR pϩR0is the response to the preferred direction,and NϭR nϩR0is the response to the nonpreferred direction.The tuning half-width is a common measure of the narrowness of orientation tuning(Campbell et al.,1968;Rose and Blakemore,1974a; Gizzi et al.,1990).It is defined as the half-width of the tuning curve at half the height of the peak.In terms of the parameters of the model,the tuning half-width is simply given bymultiplied by ln(4)1/2ϭ1.18. Coarse potentials andfiring rates.To test the rectification model offiring rate encoding,we obtained coarse membrane potential traces andfiring rates.The coarse membrane potential traces,V(t),were obtained as follows.First,we identified the time of occurrence of spikes by searching for maxima in the derivative of the membrane potential.We then identified the starting and ending times of the typical spike for each cell, including afterhyperpolarizations.Spikes typically began at t0ϭϪ1 msec(i.e.,1msec before the peak in rising potential),and ended at t1ϭ5msec(mean duration t1Ϫt0was6.5msec,ranging from2.0to12.2 msec).To remove the spikes from the traces,we replaced each[t0,t1] epoch with a line joining V(t0)to V(t1).This replacement left two small scars,i.e.,abrupt changes in the slope of the membrane potential traces at t0and t1.Subsequent low-passfiltering of the traces with cutoff frequency of24Hz made these transitions invisible.To obtain thefiring rate traces,R(t),we simply low-passfiltered the spike trains with the same cutoff frequency used with the membrane potential responses.This frequency,24Hz,is low enough that the information about the timing of the individual spikes is mostly lost.We then rectified the resultingfiring rates to remove the negative ripples introduced by low-passfiltering.RESULTSWe recorded intracellularly from41cells in the cat primary visual cortex and measured their orientation tuning with drifting sinu-soidal gratings.Twenty-nine of these cells responded with at least one spike/sec to stimuli of the preferred orientation.Twenty-Carandini and Ferster•Membrane Potential and Firing Rate in Cat V1J.Neurosci.,January1,2000,20(1):470–484471eight of these 29cells had a clear preference for orientation and are the object of this study.The mean resting potential of the cells was Ϫ63Ϯ10mV (mean ϮSD;n ϭ28).The mean spike threshold was Ϫ49Ϯ7mV.The spike height was often small compared with values commonly observed in vitro ,being on average only 21Ϯ15mV.This small value resulted from the large time constant of the electrodes,which acted as a low-pass filter.Indeed,the spike height was negatively correlated with the spike width.The latter,measured at half-height,was on average 1.6Ϯ0.9msec,but for spikes Ͼ40mV it was always Ͻ1msec.The low-pass filter did not,however,have a significant effect on visually evoked synaptic potentials,because these mostly contain substantially lower fre-quencies than spikes.Membrane potential responses to different orientationsFrom extracellular recordings,it is known that in response to drifting gratings simple and complex cells exhibit rather different spike trains:those of simple cells are strongly modulated at the stimulus frequency,whereas those of complex cells consist prin-cipally of an elevation in the mean firing rate (Movshon et al.,1978c;Skottun et al.,1991).The basis for this difference in response is often apparent when the measurements are per-formed intracellularly.This is illustrated in Figure 1,where the responses evoked by optimally oriented gratings drifting in two different directions are shown for two typical cells,one simple and one complex.The membrane potential of the simple cell (Fig.1A )was strongly modulated at the temporal frequency of the stimulus (4Hz).This modulation was stronger for the stimulus drifting in the preferred direction (left )than in the opposite direction (right ).In this cell as well as in all other simple cells in our sample,the modulation in membrane potential was seldom symmetrical around the resting potential of the cell:the membrane potential spent more time above rest than below it.Thus,together with a strong modulation,the membrane potential responses of simple cells exhibited a noticeable increase in their mean.By contrast,the membrane potential response of the complex cell (Fig.1B )consisted mainly of an elevation in the mean.Thiselevation was accompanied by a gradual hyperpolarization and reduction in spike frequency during the course of the stimulus presentation,which is most likely a consequence of pattern ad-aptation (Carandini and Ferster,1997).In addition,the mem-brane potential of the complex cell exhibited a weak modulation at the stimulus frequency (2Hz),which is most visible in the response to the nonpreferred direction.Membrane potential modulations of this sort were not a rare sight in complex cells but were in general substantially smaller than the mean increase in membrane potential.Moreover,although the membrane poten-tial response of many complex cells exhibited strong temporal variations,these temporal variations were often not synchronized with the stimulus,taking the form of seemingly random depolar-izing events of 50–500msec duration (Ferster and Carandini,1996).The effects of changing stimulus orientation on the responses of the simple cell are illustrated in Figure 2.Here the responses were averaged over each stimulus cycle,so each trace represents the average response of the cell to the passage of one bar of the grating over the receptive field.The firing rate responses (Fig.2A )are typical of many simple cells:the cell is strongly tuned for orientation,gives no response to stimuli of nonpreferred orien-tations,and displays a marked preference for one direction of motion (270°)over the opposite (90°).The strength of the tuning of the firing rate responses is only partly inherited from the underlying membrane potential re-sponses (Fig.2B )and appears to receive a substantial contribu-tion from the spike threshold.In particular,the tuning of the membrane potential responses appears to be broader than that of the firing rate responses in at least three ways.First,although stimuli at orientations flanking the preferred orientation did modulate the membrane potential and increase the mean mem-brane potential,they did not elicit firing.Second,the mean membrane potential at all orientations was more positive than in the absence of visual stimulation,an effect that is not visible in the firing rate responses (which were zero in both cases).Third,at the preferred orientation the difference between the firing rate response in the two opposite directions of motion (90and270°)Figure 1.Membrane potential re-sponses of two cells to stimuli of pre-ferred orientation drifting in the pre-ferred direction (left )and in the nonpreferred (opposite)direction (right ).A ,Responses of a simple cell (cell 61).The grating stimulus drifted at 4Hz.Each bar of the grating elicited a strong modulation in the membrane potential response.B ,Responses of a complex cell (cell 24).The grating stimulus drifted at 2Hz.The responses it elicited contained only a mild com-ponent at the stimulus frequency.The dotted horizontal lines indicate the rest-ing potential.472J.Neurosci.,January 1,2000,20(1):470–484Carandini and Ferster •Membrane Potential and Firing Rate in Cat V1was far greater than the differences between the corresponding membrane potential responses.These same observations can be made for the complex cell shown in Figure 1(Fig.3).As in the simple cell,stimuli at all orientations evoked a depolarization relative to rest.Moreover,visual stimuli at orientations surrounding the preferred orienta-tion (30and 210°)increased the mean membrane potential of the cell but did not elicit substantial firing responses,creating a substantial difference in the orientation tuning width measured from the two types of responses.Finally,the two opposite direc-tions of motion at the preferred orientation (60and 240°)elicited firing rate responses that were far more dissimilar than the corresponding membrane potential responses.Orientation selectivity of firing rate and membrane potential responsesTo quantify the responses (membrane potential or firing rate)to drifting gratings,we used two measures:mean and modulation.The first is simply the average response measured over the stim-ulus duration.The second is the peak-to-peak amplitude of the sinusoid at the grating frequency that best fits the response (i.e.,two times the amplitude of the first harmonic of the response).If the response were a perfect sinusoid,its modulation would be its peak-to-peak amplitude.The orientation tuning of the mean and modulation of both the membrane potential and the firing rate responses of thesimpleFigure 2.Cycle averages and spike histograms,as a function of stimulus orientation,for the simple cell in Figure 1A .The first column refers to a blank stimulus,and the subsequent columns refer to 12stimulus orientations,spanning the range between 0and 360°in 30°steps.Responses are averaged over one stimulus cycle (0.25sec).A ,Firing rate.B ,Membrane potential.Cell61.Figure 3.Cycle averages and spike histograms,as a function of stimulus orientation,for the complex cell in Figure 1B .Format as in Figure 2.Responses are averaged over one stimulus cycle (0.5sec).Cell 24.Carandini and Ferster •Membrane Potential and Firing Rate in Cat V1J.Neurosci.,January 1,2000,20(1):470–484473cell is illustrated in Figure 4.The modulation component was large and well tuned both in the firing rate (Fig.4B )and in the membrane potential (Fig.4D ).The mean component was much smaller but similarly tuned.For the firing rate,that the mean (Fig.4A )was tuned similarly to the modulation (Fig.4B )is simply a consequence of the lack of firing rate responses at rest.Because the resting firing rate was zero,the effect on the mean of an increase in rate in one phase of the responses could not be compensated by a decrease at another phase.For the membrane potential,by contrast,there is no corresponding constraint.Indeed,the lower limit for the mem-brane potential (the reversal potential of potassium ions)was well below the resting potential of the cells.The similarity in tuning between the mean (Fig.4C )and the modulation component (Fig.4D )is caused by the tendency pointed out in the description of Figure 1:the modulation in the membrane potential was larger above the resting potential than below it.A comparison of the orientation tuning curves for firing rate and membrane potential in Figure 4confirms that the firing rate responses are more sharply tuned than the membrane potential responses.For example,stimuli flanking the preferred orientation (240and 300°)gave membrane potential responses that were ϳ20%as large as the response at the preferred orientation (270°).Yet the firing rate responses to these stimuli were zero,indicating that the tuning width of the firing rate was smaller than the spacing between orientations (30°).In addition to the width of the tuning,the difference in tuning between membrane potential responses and firing rate responses applies most notably to the relative sizes of the responses to the two opposite directions of motion,90and 270°.Although the membrane potential responses to a grating drifting in the 270°direction are only marginallylarger than those to a grating drifting in the opposite direction,the difference in firing rate responses in the two conditions is substantial.A similar analysis in terms of mean and modulation can be performed for the complex cell of Figures 1B and 3.The results of such an analysis are illustrated in Figure 5.Consistent with the observations made on the traces,the mean component (Fig.5C )of the membrane potential response is substantially larger than the modulation component (Fig.5D ).Similarly,the mean com-ponent (Fig.5A )of the firing rate response is larger than the modulated component (Fig.5B ).In a complex cell,then,the stimulus tuning is mostly expressed in the left panels ,which report the response means.To compare the tuning of the different response measures,mean and modulation of firing rate and membrane potential,we fitted the responses with the descriptive function in Equation 1and obtained estimates of the direction index and tuning half-width (see Materials and Methods).Even in the face of the restrictions that we imposed to limit the number of free param-eters,the fits were generally good.They are illustrated by the thin curves in Figures 4and 5and in many subsequent figures.The values for the direction index confirm that for the cells in Figures 4and 5,the encoding of subthreshold events into firing rates substantially increased the selectivity for direction of mo-tion.Indeed,for the simple cell in Figure 4the direction index was 0.25for the potential modulation (Fig.4D )and 0.79for the modulation of the firing rate (Fig.4B ).For the complex cell in Figure 5the direction index was only 0.09for the mean membrane potential (Fig.5C )and 0.82for the mean firing rate (Fig.5A ).On the other hand,the values for the tuning half-width of these two cells do not suggest a substantial difference between firing rate and membrane potential in terms of orientation selectivity.Indeed,for the cell in Figure 4the tuning half-width was 18°for the firing rate and 21°for the membrane potential,and for the cell in Figure 5the tuning half-width was similarly narrow in the two signals (17°).Before concluding that in these cells the encoding of membrane potential into firing rates did not sharpen the tuning,however,Figure 4.Orientation tuning of the simple cell in Figures 1A and 2.Top ,Firing rate.Bottom ,Membrane potential.Left ,Mean responses.Right ,Response modulation.Gray areas indicate confidence intervals for the responses to a blank stimulus.Their width and the length of the error bars on the data points are twice the SE of the measurements.In the top panels the confidence intervals are infinitesimal:the response to the blank was always 0spikes/sec.The thin curves indicate the fits of a descriptive tuning curve (Eq.1).The thick lines in the top panels indicate the predictions of the rectification model of firing rate,obtained from the membrane po-tential responses.Cell61.Figure 5.Orientation tuning of the complex cell of Figures 1B and 3.Format as in Figure 4.Cell 24.474J.Neurosci.,January 1,2000,20(1):470–484Carandini and Ferster •Membrane Potential and Firing Rate in Cat V1one should consider that half-widths of 17–18°are the lowest that can be measured from our data.This limit arises from the 30°spacing of our stimuli on the orientation axis.Because in these two cells the firing rate responses were zero at all orientations except the preferred,it is likely that the true tuning half-width for the firing rate was actually Ͻ17°.For the membrane potential,on the other hand,the presence of data points on the slopes of the tuning curves (Figs.4D ,5C )indicates that the data would not be fitted by narrower tuning curves.The difference in tuning sharpness between the membrane potential and the firing rate is most evident in cells that are more broadly tuned,where our sampling limitations do not play a role.This is illustrated in Figure 6,which contains the tuning curves for four additional cells,two complex and two simple.For three of these cells,the orientation tuning of the firing rate responses was significantly sharper than that of the membrane potential responses.These are the first complex cell (Fig.6A–D ,half-widths of 23°for the firing rate and 40°for themembraneFigure 6.Orientation tunings of two complex cells and two simple cells.The format of each group of four panels is as in Figure 4.A–D,E–G ,Complex cells (cells 86and 28).I–L,M–P ,Simple cells (cells 68and 71).These cells are arranged in order of spike modulation index:0.88,0.92,1.43,and 1.54.The corresponding potential modulation indices are 0.41,0.37,0.56,and 1.84.Carandini and Ferster •Membrane Potential and Firing Rate in Cat V1J.Neurosci.,January 1,2000,20(1):470–484475。