"""S-300 Basic water-only drying: conservative cohorts, explicitly uncalibrated.""" from __future__ import annotations import copy,json,math from asset_runtime import _annotations as _ann from pathlib import Path from asset_runtime.mt_hx204 import ActionRejected,number,obj,BOOL,TEXT from asset_runtime.antonpaar_abbematadvanced import validate ROOT=Path(__file__).resolve().parents[2];ASSET_TYPE_ID='instrument.buchi_minispray';CATALOG_ID='CHEM-026';PROTOCOL_VERSION='1.0.0';TEMPLATE_REL='assets/reactions/buchi_minispray_drying_library/templates.json' PHASE={'type':'string','enum':['idle','running','succeeded','cancelled','failed']} def arr(s):return {'type':'array','items':s} def nullable(s):return {'anyOf':[s,{'type':'null'}]} MASS=number('kg',0);FRAC=number('1',0,1);TEMP=number('K',200,700);FLOW=number('m^3/s',.1e-6/60,30e-6/60) PLANT=obj({'ambient_k':number('K',278.15,313.15),'gas_reference_k':number('K',273.15,313.15),'gas_reference_pa':number('Pa',80000,120000),'gas_density_kg_m3':number('kg/m^3',.5,2),'gas_cp_j_kg_k':number('J/kg/K',700,1500),'heater_power_w':number('W',1,2300),'auxiliary_power_w':number('W',1,2300),'thermal_tau_s':number('s',.5,600),'chamber_volume_m3':number('m^3',.0001,.03),'water_density_kg_m3':number('kg/m^3',900,1100),'latent_j_kg':number('J/kg',2e6,2.6e6),'max_humidity_gain_kg_kg':number('kg/kg',.001,.5),'d2_rate_m2_s':number('m^2/s',1e-13,1e-7),'wall_rate_s_inv':number('1/s',0,10),'cyclone_d50_m':number('m',1e-7,1e-4),'filter_efficiency':FRAC,'filter_resistance_pa_kg':number('Pa/kg',0,1e10),'gas_supply_pa':number('Pa',6.5e5,7e5),'gas_pressure_basis':{'type':'string','enum':['manufacturer_unspecified']},'gas_connected':BOOL,'recipe_reviewed':BOOL,'coefficient_evidence':TEXT}) EXAMPLE=dict(ambient_k=298.15,gas_reference_k=298.15,gas_reference_pa=101325.,gas_density_kg_m3=1.184,gas_cp_j_kg_k=1005.,heater_power_w=2000.,auxiliary_power_w=300.,thermal_tau_s=3.,chamber_volume_m3=.008,water_density_kg_m3=997.,latent_j_kg=2.3e6,max_humidity_gain_kg_kg=.1,d2_rate_m2_s=3e-9,wall_rate_s_inv=.04,cyclone_d50_m=4e-6,filter_efficiency=.95,filter_resistance_pa_kg=1e7,gas_supply_pa=6.7e5,gas_pressure_basis='manufacturer_unspecified',gas_connected=True,recipe_reviewed=True,coefficient_evidence='synthetic_host_parameters_not_S300_calibration') SAMPLE=obj({'sample_id':TEXT,'substance_id':TEXT,'solvent':{'type':'string','enum':['water']},'volume_m3':number('m^3',1e-9,.01),'solid_mass_fraction':number('1',.001,.5),'solid_density_kg_m3':number('kg/m^3',200,5000),'damage_rate_ref_s_inv':number('1/s',0,100),'damage_reference_k':TEMP,'damage_activation_j_mol':number('J/mol',0,2e5),'sticky_temperature_k':TEMP,'homogeneous_feed_reviewed':BOOL}) SAMPLE_EXAMPLE=dict(sample_id='feed_1',substance_id='d_lactose',solvent='water',volume_m3=50e-6,solid_mass_fraction=.1,solid_density_kg_m3=1500.,damage_rate_ref_s_inv=.001,damage_reference_k=350.,damage_activation_j_mol=40000.,sticky_temperature_k=360.,homogeneous_feed_reviewed=True) METHOD=obj({'inlet_target_k':number('K',303.15,493.15),'feed_m3_s':FLOW,'drying_gas_m3_s':number('m^3/s',1e-4,35/3600),'spray_gas_m3_s':number('m^3/s',80e-3/3600,1800e-3/3600),'nozzle':{'type':'string','enum':['two_fluid']},'needle_diameter_m':{'type':'number','enum':[.0005,.0007,.0014,.002],'x-unit':'m'},'atom_d_ref_m':number('m',1e-6,200e-6),'atom_reference_feed_m3_s':FLOW,'atom_reference_gas_m3_s':number('m^3/s',80e-3/3600,1800e-3/3600)}) METHOD_EXAMPLE=dict(inlet_target_k=423.15,feed_m3_s=5e-6/60,drying_gas_m3_s=25/3600,spray_gas_m3_s=600e-3/3600,nozzle='two_fluid',needle_diameter_m=.0007,atom_d_ref_m=30e-6,atom_reference_feed_m3_s=5e-6/60,atom_reference_gas_m3_s=600e-3/3600) POINT=obj({'time_s':number('s',0),'inlet_k':TEMP,'outlet_k':TEMP,'feed_m3_s':number('m^3/s',0),'evaporation_kg_s':number('kg/s',0),'filter_delta_pa':number('Pa',0)}) RESULT=obj({'phase':PHASE,'fault':TEXT,'inlet_k':nullable(TEMP),'outlet_k':nullable(TEMP),'product_gas_temperature_k':{'type':'null'},'drying_gas_m3_s':number('m^3/s',0),'evaporation_kg_s':number('kg/s',0),'filter_delta_pa':number('Pa',0),'filter_maintenance_due':BOOL,'evidence':TEXT}) PRODUCT=obj({'sample_id':TEXT,'dry_solids_kg':MASS,'water_kg':MASS,'yield_dry_solid_fraction':nullable(FRAC),'active_fraction':nullable(FRAC),'water_mass_fraction':nullable(FRAC),'mass_weighted_particle_diameter_m':nullable(number('m',0)),'wet_reject_kg':MASS,'wall_mass_kg':MASS,'filter_mass_kg':MASS,'exhaust_particle_mass_kg':MASS,'evidence':TEXT,'template_source':TEXT}) REFERENCE=obj({'substance_id':TEXT,'glass_former':BOOL,'stable_on_storage':nullable(BOOL),'glass_transition_k':TEMP,'melting_k':TEMP,'tg_evidence':TEXT,'conditions':TEXT,'source':TEXT,'template_source':TEXT,'s300_yield_fraction':{'type':'null'},'s300_particle_diameter_m':{'type':'null'},'evidence':TEXT}) CAPS={ 'power.set':(obj({'enabled':BOOL}),obj({'enabled':BOOL}),['power_inlet'],'供电;断电停泵停气但库存不消失','device_command','agent',{'enabled':True},['power.enabled','cycle.phase']), 'clamp.set_lift':(obj({'lift_m':number('m',0,.03)}),obj({'lift_m':number('m',0,.03)}),['cylinder_clamp'],'教学夹具行程,冷却停气后才允许拆装','device_command','agent',{'lift_m':.03},['clamp.lift_m']), 'vessel.set_lower':(obj({'lower_m':number('m',0,.05)}),obj({'lower_m':number('m',0,.05)}),['collection_vessel'],'教学集粉瓶拆卸行程','device_command','agent',{'lower_m':.05},['vessel.lower_m']), 'plant.configure':(PLANT,obj({'configured':BOOL}),['heater','aspirator','outlet_filter'],'宿主首次物理系数与气源审查','configuration','evaluator',EXAMPLE,['plant.configured']), 'sample.configure':(SAMPLE,obj({'configured':BOOL,'attachment_event':TEXT}),['feed_port'],'宿主水系单固体样品,一实例一批次','configuration','evaluator',SAMPLE_EXAMPLE,['sample.configured']), 'method.configure':(METHOD,obj({'configured':BOOL}),['feed_pump','nozzle','heater'],'Basic两流体方法;雾化粒径系数为宿主假设','configuration','evaluator',METHOD_EXAMPLE,['method.configured']), 'drying.prepare':(obj({}),obj({'preparing':BOOL}),['heater','aspirator','nozzle'],'启动气流和加热,必须step达到温度','device_command','agent',{},['airflow.enabled','heater.enabled']), 'acquisition.start':(obj({}),obj({'phase':PHASE,'operation_id':TEXT}),['feed_pump','spray_cylinder','cyclone'],'启动/续作,料液耗尽后排空飞行颗粒才完成','device_command','agent',{},['cycle.phase']), 'acquisition.stop':(obj({}),obj({'phase':PHASE}),['feed_pump'],'取消进料,不冻结热过程或飞行颗粒','device_command','agent',{},['cycle.phase']), 'drying.shutdown':(obj({}),obj({'cooling':BOOL}),['heater','aspirator'],'停加热保留抽气冷却,不自动清洗','device_command','agent',{},['heater.enabled','cycle.phase']), 'airflow.stop':(obj({}),obj({'stopped':BOOL}),['aspirator'],'冷却且无飞行颗粒才能停止抽气','device_command','agent',{},['airflow.enabled']), 'drying.measure':(obj({}),RESULT,['display_panel'],'当前气温流量压差;不把可选产品气温当颗粒温度','query','agent',{},[]), 'product.read':(obj({}),PRODUCT,['collection_vessel'],'未标定产率/湿度/粒径/活性真值;非实测','query','evaluator',{},[]), 'history.read':(obj({}),obj({'records':arr(POINT),'truncated':BOOL,'evidence':TEXT}),['display_panel'],'每秒过程记录,读取不推进','query','agent',{},[]), 'reference.lookup':(obj({'substance_id':TEXT}),REFERENCE,['display_panel'],'50物质原条件参考,不外推S300粒度产率','query','agent',{'substance_id':'d_lactose'},[]), 'product.unload':(obj({'sample_id':TEXT}),obj({'unloaded':BOOL,'attachment_event':TEXT}),['collection_vessel'],'冷却、停气、降瓶后宿主取出产品','configuration','evaluator',{'sample_id':'feed_1'},['truth.removed_mass_kg'])} SLOTS={} def slot(k,s,u,o='derived',v='agent',c='display_panel',w=None):SLOTS[k]=(s,u,o,v,[c],w) slot('power.enabled',BOOL,'1','setpoint',c='power_inlet',w=('power.set','enabled'));slot('clamp.lift_m',number('m',0,.03),'m','scene',c='cylinder_clamp',w=('clamp.set_lift','lift_m'));slot('vessel.lower_m',number('m',0,.05),'m','scene',c='collection_vessel',w=('vessel.set_lower','lower_m')) for k,s,u in [('plant.configured',BOOL,'1'),('sample.configured',BOOL,'1'),('method.configured',BOOL,'1'),('cycle.phase',PHASE,'1'),('cycle.fault',TEXT,'1'),('cycle.elapsed_s',number('s',0),'s'),('airflow.enabled',BOOL,'1'),('heater.enabled',BOOL,'1'),('thermal.inlet_k',nullable(TEMP),'K'),('thermal.outlet_k',nullable(TEMP),'K'),('flow.drying_m3_s',number('m^3/s',0),'m^3/s'),('flow.feed_m3_s',number('m^3/s',0),'m^3/s'),('evaporation.kg_s',number('kg/s',0),'kg/s'),('filter.delta_pa',number('Pa',0),'Pa')]:slot(k,s,u) for k in ['input','retained','vapor','removed','product','wall','filter','exhaust','wet_reject']:slot('truth.'+k+'_mass_kg',MASS,'kg','process_truth','evaluator','spray_cylinder') class BuchiMinisprayRuntime: def __init__(self,instance_id='minispray_01'): self.instance_id=instance_id;self.time_s=0.;self.revision=0;self.powered=False;self.lift=0.;self.lower=0.;self.plant=None;self.sample=None;self.method=None;self.phase='idle';self.fault='';self.elapsed_s=0.;self.operation_id=None;self._operation_count=0;self.airflow=False;self.heating=False;self.inlet=298.15;self.outlet=298.15;self.stock={'s':0.,'w':0.,'a':0.};self.bins=[];self.pools={k:dict(s=0.,w=0.,a=0.) for k in ['product','wall','filter','exhaust','wet_reject','removed']};self.input_mass=0.;self.initial_solid=0.;self.vapor=0.;self.evap_rate=0.;self.dp=0.;self.diameter_sum=0.;self.unloaded=False;self.history=[];self.history_truncated=False;self.next_sample=0.;self.templates={t['substance_id']:t for t in json.loads((ROOT/TEMPLATE_REL).read_text())['templates']};self._principals={'__public_agent__':'agent'};self._requests={};self._owners={} def register_principal(self,principal_id,visibility='agent'): if visibility not in ('agent','evaluator','debug'):raise ActionRejected('INVALID_ARGUMENT') if principal_id in self._principals:raise ActionRejected('REQUEST_CONFLICT') self._principals[principal_id]=visibility def session(self,principal_id='__public_agent__'): if principal_id not in self._principals:raise ActionRejected('ACCESS_DENIED') return BuchiMinispraySession(self,principal_id) def describe(self):return self.session().describe(instance_id=self.instance_id) @staticmethod def mass(p):return p['s']+p['w'] def _inventory(self): v={k:self.mass(p) for k,p in self.pools.items()};return dict(input=self.input_mass,vapor=self.vapor,retained=self.mass(self.stock)+sum(self.mass(b) for b in self.bins)+sum(v[k] for k in ('product','wall','filter','wet_reject')),**{k:v[k] for k in v}) def _values(self): v={'power.enabled':self.powered,'clamp.lift_m':self.lift,'vessel.lower_m':self.lower,'plant.configured':self.plant is not None,'sample.configured':self.sample is not None,'method.configured':self.method is not None,'cycle.phase':self.phase,'cycle.fault':self.fault,'cycle.elapsed_s':self.elapsed_s,'airflow.enabled':self.airflow,'heater.enabled':self.heating,'thermal.inlet_k':self.inlet if self.powered else None,'thermal.outlet_k':self.outlet if self.powered else None,'flow.drying_m3_s':self.method['drying_gas_m3_s'] if self.airflow else 0.,'flow.feed_m3_s':self.method['feed_m3_s'] if self.phase=='running' and self.mass(self.stock)>1e-18 else 0.,'evaporation.kg_s':self.evap_rate,'filter.delta_pa':self.dp};v.update({'truth.'+k+'_mass_kg':x for k,x in self._inventory().items()});return v def read(self,visibility='agent'):return copy.deepcopy({k:v for k,v in self._values().items() if SLOTS[k][3]=='agent' or visibility in ('evaluator','debug')}) def debug_snapshot(self):return copy.deepcopy(dict(state=self.read('evaluator'),stock=self.stock,bins=self.bins,pools=self.pools)) def _measure(self):return dict(phase=self.phase,fault=self.fault,inlet_k=self.inlet if self.powered else None,outlet_k=self.outlet if self.powered else None,product_gas_temperature_k=None,drying_gas_m3_s=self.method['drying_gas_m3_s'] if self.airflow else 0.,evaporation_kg_s=self.evap_rate,filter_delta_pa=self.dp,filter_maintenance_due=self.dp>2000.,evidence='synthetic_host_drying_model; gas temperatures, no optional product sensor') def _product(self): p=self.pools['removed'] if self.unloaded else self.pools['product'];m=self.mass(p);return dict(sample_id=self.sample['sample_id'] if self.sample else '',dry_solids_kg=p['s'],water_kg=p['w'],yield_dry_solid_fraction=p['s']/self.initial_solid if self.initial_solid else None,active_fraction=p['a']/p['s'] if p['s'] else None,water_mass_fraction=p['w']/m if m else None,mass_weighted_particle_diameter_m=self.diameter_sum/p['s'] if p['s'] else None,wet_reject_kg=self.mass(self.pools['wet_reject']),wall_mass_kg=self.mass(self.pools['wall']),filter_mass_kg=self.mass(self.pools['filter']),exhaust_particle_mass_kg=self.mass(self.pools['exhaust']),evidence='synthetic_conservative_cohort_model; NOT S300 measured yield or morphology',template_source=TEMPLATE_REL) def invoke(self,capability,**a): if capability not in CAPS:raise ActionRejected('UNKNOWN_CAPABILITY') validate(CAPS[capability][0],a) if self.phase=='running' and CAPS[capability][4]!='query' and capability not in ('power.set','acquisition.stop','drying.shutdown'):raise ActionRejected('BUSY') if capability=='power.set': self.powered=a['enabled'] if not self.powered: self.airflow=False;self.heating=False if self.phase=='running':self.phase='cancelled' out=a elif capability in ('clamp.set_lift','vessel.set_lower'): ta=self.plant['ambient_k'] if self.plant else 298.15 if self.airflow or self.heating or self.bins or self.inlet>ta+5:raise ActionRejected('PRECONDITION_FAILED') if capability=='clamp.set_lift':self.lift=a['lift_m'] else:self.lower=a['lower_m'] out=a elif capability=='plant.configure': if self.plant or self.sample or not a['recipe_reviewed'] or not a['gas_connected'] or a['heater_power_w']+a['auxiliary_power_w']>2300 or not a['coefficient_evidence']:raise ActionRejected('PRECONDITION_FAILED') self.plant=copy.deepcopy(a);self.inlet=self.outlet=a['ambient_k'];out={'configured':True} elif capability=='sample.configure': if not self.plant or self.sample or self.phase!='idle' or not a['sample_id'] or a['substance_id'] not in self.templates or not a['homogeneous_feed_reviewed']:raise ActionRejected('PRECONDITION_FAILED') f=a['solid_mass_fraction'];rho=1/(f/a['solid_density_kg_m3']+(1-f)/self.plant['water_density_kg_m3']);m=rho*a['volume_m3'];self.stock=dict(s=m*f,w=m*(1-f),a=m*f);self.input_mass=m;self.initial_solid=m*f;self.sample=copy.deepcopy(a);out=dict(configured=True,attachment_event='host_attach:'+a['sample_id']) elif capability=='method.configure': if not self.plant or self.airflow or self.bins or self._operation_count:raise ActionRejected('PRECONDITION_FAILED') self.method=copy.deepcopy(a);out={'configured':True} elif capability=='drying.prepare': if not self.powered or not self.plant or not self.method or self.lift>1e-9 or self.lower>1e-9:raise ActionRejected('PRECONDITION_FAILED') self.airflow=True;self.heating=True;out={'preparing':True} elif capability=='acquisition.start': if not self.powered or not self.heating or not self.airflow or not self.sample or self.unloaded or self.lift>1e-9 or self.lower>1e-9 or self.phase=='failed' or abs(self.inlet-self.method['inlet_target_k'])>3 or (self.mass(self.stock)<1e-18 and not self.bins):raise ActionRejected('PRECONDITION_FAILED') self.phase='running';self._operation_count+=1;self.operation_id=self.instance_id+':'+str(self._operation_count);out=dict(phase=self.phase,operation_id=self.operation_id) elif capability=='acquisition.stop': if self.phase!='running':raise ActionRejected('PRECONDITION_FAILED') self.phase='cancelled';out=dict(phase=self.phase) elif capability=='drying.shutdown': self.heating=False if self.phase=='running':self.phase='cancelled' out=dict(cooling=self.airflow) elif capability=='airflow.stop': if self.heating or self.bins or (self.plant and self.inlet>self.plant['ambient_k']+5):raise ActionRejected('PRECONDITION_FAILED') self.airflow=False;out={'stopped':True} elif capability=='drying.measure':return self._measure() elif capability=='product.read':return self._product() elif capability=='history.read':return dict(records=copy.deepcopy(self.history),truncated=self.history_truncated,evidence='synthetic model 1s snapshots; not manufacturer recorded trace') elif capability=='reference.lookup': t=self.templates.get(a['substance_id']) if not t:raise ActionRejected('TEMPLATE_RANGE_UNAVAILABLE') v=t['values'];return dict(substance_id=t['substance_id'],glass_former=v['glass_former'],stable_on_storage=v['stable_on_storage'],glass_transition_k=v['glass_transition_k'],melting_k=v['melting_k'],tg_evidence=t['quantity_evidence']['glass_transition_k'],conditions=json.dumps(t['conditions'],sort_keys=True),source=t['source'],template_source=TEMPLATE_REL,s300_yield_fraction=None,s300_particle_diameter_m=None,evidence=t['evidence']) elif capability=='product.unload': if not self.sample or a['sample_id']!=self.sample['sample_id'] or self.unloaded or self.phase not in ('succeeded','cancelled') or self.airflow or self.heating or self.bins or self.lower<.049 or self.inlet>self.plant['ambient_k']+5:raise ActionRejected('PRECONDITION_FAILED') self.pools['removed']=self.pools['product'];self.pools['product']=dict(s=0.,w=0.,a=0.);self.unloaded=True;out=dict(unloaded=True,attachment_event='host_release:'+a['sample_id']) self.revision+=1;return copy.deepcopy(out) def _diameter(self,b):return (6*(b['w']/self.plant['water_density_kg_m3']+b['s']/self.sample['solid_density_kg_m3'])/(math.pi*b['n']))**(1/3) if b['n'] else 0. def _transfer(self,b,key,f): p=self.pools[key];f=min(1.,max(0.,f));d=self._diameter(b) if key=='product':self.diameter_sum+=b['s']*f*d for k in ['s','w','a']:x=b[k]*f;p[k]+=x;b[k]-=x b['n']*=1-f def _tick(self,h): p=self.plant;ta=p['ambient_k'];m=self.method;gas=m['drying_gas_m3_s']+m['spray_gas_m3_s'] if self.airflow else 0.;mdot=gas*p['gas_density_kg_m3'];cp=p['gas_cp_j_kg_k'];target=min(m['inlet_target_k'],ta+p['heater_power_w']/max(mdot*cp,1e-12)) if self.heating and self.airflow else ta self.inlet+=(target-self.inlet)*-math.expm1(-h/p['thermal_tau_s']);self.evap_rate=0. if self.phase=='running' and self.mass(self.stock)>1e-18: rho=1/(self.sample['solid_mass_fraction']/self.sample['solid_density_kg_m3']+(1-self.sample['solid_mass_fraction'])/p['water_density_kg_m3']);fraction=min(1.,m['feed_m3_s']*rho*h/self.mass(self.stock));feed={k:self.stock[k]*fraction for k in ['s','w','a']} for k in feed:self.stock[k]-=feed[k] dref=m['atom_d_ref_m']*(m['feed_m3_s']/m['atom_reference_feed_m3_s'])**.25*(m['atom_reference_gas_m3_s']/m['spray_gas_m3_s'])**.35*(m['needle_diameter_m']/.0007)**.5 for ds,f in [(.65,.25),(1.,.5),(1.6,.25)]: b={k:feed[k]*f for k in feed};b.update(age=0.,n=6*(b['w']/p['water_density_kg_m3']+b['s']/self.sample['solid_density_kg_m3'])/(math.pi*(dref*ds)**3));self.bins.append(b) proposals=[] for b in self.bins: d=self._diameter(b);ddry=(6*b['s']/self.sample['solid_density_kg_m3']/math.pi/b['n'])**(1/3) if b['n'] else 0.;dnew=math.sqrt(max(ddry**2,d*d-p['d2_rate_m2_s']*max(0.,self.inlet-ta)/50*h)) if self.airflow else d wnew=max(0.,(dnew**3-ddry**3)*math.pi*b['n']/6*p['water_density_kg_m3']);proposals.append(min(b['w'],max(0.,b['w']-wnew))) requested=sum(proposals);energy=mdot*cp*max(0.,self.inlet-ta)*h;limit=min(energy/p['latent_j_kg'],mdot*p['max_humidity_gain_kg_kg']*h);scale=min(1.,limit/requested) if requested else 0.;evap=requested*scale;self.vapor+=evap;self.evap_rate=evap/h;self.outlet=self.inlet-evap*p['latent_j_kg']/max(h*mdot*cp,1e-12) if self.airflow else self.inlet keep=[];qactual=gas*self.inlet/p['gas_reference_k'];residence=p['chamber_volume_m3']/qactual if qactual else math.inf for b,e in zip(self.bins,proposals): b['w']-=e*scale;wet=b['w']/max(self.mass(b),1e-30);tp=ta+(self.outlet-ta)*(.3 if wet>.02 else 1.);s=self.sample;rate=s['damage_rate_ref_s_inv']*math.exp(max(-60.,min(60.,s['damage_activation_j_mol']/8.314462618*(1/s['damage_reference_k']-1/tp))));b['a']*=math.exp(-rate*h) if self.airflow: b['age']+=h;wall=p['wall_rate_s_inv']*(1+4*(wet>.15)+2*(tp>s['sticky_temperature_k']));self._transfer(b,'wall',-math.expm1(-wall*h)) if b['age']>=residence: if wet>.15:self._transfer(b,'wet_reject',1.) else: d=self._diameter(b);cut=p['cyclone_d50_m']/math.sqrt(m['drying_gas_m3_s']/(25/3600));eta=d*d/(d*d+cut*cut);self._transfer(b,'product',eta);self._transfer(b,'filter',p['filter_efficiency']);self._transfer(b,'exhaust',1.) continue if self.mass(b)>1e-30:keep.append(b) self.bins=keep;self.dp=p['filter_resistance_pa_kg']*self.mass(self.pools['filter'])*(m['drying_gas_m3_s']/(25/3600)) if self.airflow else 0. if self.phase=='running': self.elapsed_s+=h if self.mass(self.stock)<=1e-18 and not self.bins:self.phase='succeeded' self.time_s+=h if self.time_s+1e-12>=self.next_sample: point=dict(time_s=self.time_s,inlet_k=self.inlet,outlet_k=self.outlet,feed_m3_s=self._values()['flow.feed_m3_s'],evaporation_kg_s=self.evap_rate,filter_delta_pa=self.dp) if len(self.history)<10000:self.history.append(point) else:self.history_truncated=True self.next_sample=self.time_s+1. def step(self,dt): if isinstance(dt,bool) or not isinstance(dt,(int,float)) or not math.isfinite(dt) or not 0