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5f2f48d d1292d8 5f2f48d d1292d8 5f2f48d d1292d8 5f2f48d d1292d8 5f2f48d d1292d8 5f2f48d | 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 134 135 136 137 138 139 140 141 142 143 144 145 146 147 148 149 150 151 152 153 154 155 156 157 158 159 160 161 162 163 164 165 166 167 168 169 170 171 172 173 174 175 176 177 178 179 180 181 182 183 184 185 186 187 188 189 190 191 192 193 194 195 196 197 198 199 200 201 202 203 204 205 206 207 208 209 210 211 212 213 214 215 216 217 218 219 220 221 222 223 224 225 226 227 228 229 230 231 232 233 234 235 236 237 238 239 240 241 242 243 244 245 246 247 248 249 250 251 252 253 254 255 256 257 258 259 260 261 262 263 264 265 266 267 268 269 270 271 272 273 274 275 276 277 278 279 280 281 282 283 284 285 286 287 288 289 290 291 292 293 294 295 296 297 298 299 300 301 302 303 304 305 306 307 308 309 310 311 312 313 314 315 316 317 318 319 320 321 322 323 324 325 326 327 328 329 330 331 332 333 334 335 336 337 338 339 340 341 342 343 344 345 346 347 348 349 350 351 352 353 354 355 356 357 358 359 360 361 362 363 364 365 366 367 368 369 370 371 372 373 374 375 376 377 378 379 380 381 382 383 384 385 386 387 388 389 390 391 392 393 394 395 396 397 398 399 400 401 402 403 404 405 406 | """CHEM-116 finite mercury intrusion with measured branches and explicit transfer uncertainty."""
from pathlib import Path
import copy,math,json,importlib.util
PROTOCOL_VERSION='1.0.0';SLUG='antonpaar_poremaster60';CATALOG_ID='CHEM-116';ASSET_TYPE_ID='instrument.'+SLUG
ROOT=Path(__file__).resolve().parents[2];ASSET=ROOT/'assets/expansion_batch03/t4_measure'/SLUG
class ActionRejected(ValueError):pass
def number(unit='1',lo=None,hi=None):
d={'type':'number','x-unit':unit}
if lo is not None:d['minimum']=lo
if hi is not None:d['maximum']=hi
return d
def obj(p):return dict(type='object',properties=p,required=list(p),additionalProperties=False)
def arr(v,n=None):
d=dict(type='array',items=v)
if n is not None:d.update(minItems=n,maxItems=n)
return d
def nullable(s):return {'anyOf':[s,{'type':'null'}]}
def enum(v):return {'type':'string','enum':v}
TEXT={'type':'string'};BOOL={'type':'boolean'};PHASE=enum(['idle','running','succeeded','cancelled','failed'])
def validate(s,v):
if 'anyOf' in s:
for q in s['anyOf']:
try:validate(q,v);return
except ActionRejected:pass
raise ActionRejected('INVALID_ARGUMENT')
t=s.get('type')
if t in ('number','integer'):
if isinstance(v,bool) or not isinstance(v,(int,float)) or not math.isfinite(v) or (t=='integer' and type(v) is not int) or not s.get('minimum',-math.inf)<=v<=s.get('maximum',math.inf):raise ActionRejected('INVALID_ARGUMENT')
elif t=='boolean' and type(v) is not bool:raise ActionRejected('INVALID_ARGUMENT')
elif t=='string' and not isinstance(v,str):raise ActionRejected('INVALID_ARGUMENT')
elif t=='null' and v is not None:raise ActionRejected('INVALID_ARGUMENT')
elif t=='object':
if not isinstance(v,dict) or not set(s.get('required',[]))<=v.keys() or set(v)-set(s['properties']):raise ActionRejected('INVALID_ARGUMENT')
for k,x in v.items():validate(s['properties'][k],x)
elif t=='array':
if not isinstance(v,list) or not s.get('minItems',0)<=len(v)<=s.get('maxItems',math.inf):raise ActionRejected('INVALID_ARGUMENT')
for x in v:validate(s['items'],x)
if 'enum' in s and v not in s['enum']:raise ActionRejected('INVALID_ARGUMENT')
import bisect
DT=.1;R=8.314462618;PSI=6894.757293168;AMBIENT=101325.;P_MAX=60000*PSI
LIB=json.loads((ASSET/'porosimetry_library.json').read_text());SID='hemp_shiv'
INT=lambda lo,hi:dict(number('1',lo,hi),type='integer')
PLANT=obj({'temperature_k':number('K',283.15,313.15),'source_volume_m3':number('m^3',1e-5,.1),'source_pressure_pa':number('Pa',50*PSI,1e6),'gas_rate_s':number('1/s',.1,20),'pump_rate_s':number('1/s',.1,20),'chamber_volume_m3':number('m^3',1e-6,.01),'oil_volume_m3':number('m^3',1e-7,.01),'hp_dead_volume_m3':number('m^3',1e-6,.001),'oil_bulk_modulus_pa':number('Pa',1e8,1e10),'oil_flow_m3_s':number('m^3/s',1e-10,1e-4),'intrusion_rate_s':number('1/s',.01,10),'hg_density_kg_m3':number('kg/m^3',13000,14000),'hg_bulk_modulus_pa':number('Pa',1e9,1e11),'glass_compliance_m3_pa':number('m^3/Pa',0,1e-15),'capacitance_volume_factor_m3_f':number('m^3/F',1000,100000),'capacitance_offset_f':number('F',-1e-9,1e-9),'pressure_gain':arr(number('1',.8,1.2),3),'pressure_offset_pa':arr(number('Pa',-1e5,1e5),3),'accept_engineering_model':BOOL})
PLANT_EXAMPLE=dict(temperature_k=292.05,source_volume_m3=.002,source_pressure_pa=600000.,gas_rate_s=5.,pump_rate_s=8.,chamber_volume_m3=.0001,oil_volume_m3=.0002,hp_dead_volume_m3=.0001,oil_bulk_modulus_pa=1.4e9,oil_flow_m3_s=2e-6,intrusion_rate_s=2.,hg_density_kg_m3=13548.9,hg_bulk_modulus_pa=2.85e10,glass_compliance_m3_pa=1e-18,capacitance_volume_factor_m3_f=20000.,capacitance_offset_f=1e-12,pressure_gain=[1.]*3,pressure_offset_pa=[0.]*3,accept_engineering_model=True)
SAMPLE=obj({'sample_id':TEXT,'reference_id':TEXT,'true_dry_mass_kg':number('kg',1e-8,.1),'true_bulk_volume_m3':number('m^3',1e-10,18e-6),'dry':BOOL,'accept_cross_instrument_transfer':BOOL})
SAMPLE_EXAMPLE=dict(sample_id='hemp_01',reference_id=SID,true_dry_mass_kg=.0000655,true_bulk_volume_m3=.0000655/306.1,dry=True,accept_cross_instrument_transfer=True)
METHOD=obj({'stage':enum(['low','high']),'pressures_pa':arr(number('Pa',.2*PSI,P_MAX)),'pressure_rate_pa_s':number('Pa/s',1,2e8),'equilibration_s':number('s',.2,300),'pressure_tolerance_pa':number('Pa',.1,30000),'max_volume_drift_m3_s':number('m^3/s',1e-15,1e-7),'point_timeout_s':number('s',1,7200),'entered_mass_kg':number('kg',1e-8,.1),'closure_m3_kg':number('m^3/kg',0,.1),'surface_tension_n_m':number('N/m',.4,.6),'advancing_angle_rad':number('rad',math.pi/2+.01,math.pi),'receding_angle_rad':number('rad',math.pi/2+.01,math.pi)})
METHOD_EXAMPLE=dict(stage='low',pressures_pa=[3*PSI,10*PSI,30*PSI,50*PSI],pressure_rate_pa_s=50000.,equilibration_s=2.,pressure_tolerance_pa=15.,max_volume_drift_m3_s=1e-12,point_timeout_s=180.,entered_mass_kg=.0000655,closure_m3_kg=0.,surface_tension_n_m=.48,advancing_angle_rad=140*math.pi/180,receding_angle_rad=140*math.pi/180)
PCAL=obj({'range_index':INT(0,2),'reference_pa':arr(number('Pa',0,P_MAX),2),'measured_pa':arr(number('Pa',-1e5,1.3*P_MAX),2)})
PCAL_EXAMPLE=dict(range_index=0,reference_pa=[0.,50*PSI],measured_pa=[0.,50*PSI])
VCAL=obj({'reference_volume_m3':arr(number('m^3',0,2e-6),2),'measured_capacitance_f':arr(number('F',-1e-9,1e-9),2)})
VCAL_EXAMPLE=dict(reference_volume_m3=[0.,.2e-6],measured_capacitance_f=[1e-12,11e-12])
BLANK=obj({'pressures_pa':arr(number('Pa',0,P_MAX)),'volumes_m3':arr(number('m^3',-1e-6,1e-6))})
POINT=obj({'time_s':number('s',0),'stage':enum(['low','high']),'branch':enum(['intrusion','extrusion']),'pressure_pa':number('Pa',0),'intrusion_volume_m3':number('m^3'),'specific_volume_m3_kg':number('m^3/kg'),'corrected_pore_volume_m3_kg':number('m^3/kg',0),'diameter_m':nullable(number('m',0))})
PSD=obj({'diameter_m':arr(number('m',0)),'incremental_volume_m3_kg':arr(number('m^3/kg')),'differential_log_volume_m3_kg':arr(number('m^3/kg')),'status':TEXT})
RESULT=obj({'template_source':TEXT,'evidence':TEXT,'phase':PHASE,'stage':TEXT,'elapsed_s':number('s',0),'points':arr(POINT),'distribution':PSD,'max_pore_volume_m3_kg':nullable(number('m^3/kg',0)),'warnings':arr(TEXT)})
LEDGER=obj({'hg_added_kg':number('kg',0),'hg_stock_kg':number('kg',0),'hg_free_in_cell_kg':number('kg',0),'hg_intruded_kg':number('kg',0),'hg_waste_kg':number('kg',0),'hg_returned_with_sample_kg':number('kg',0),'hg_residual_kg':number('kg'),'solid_loaded_kg':number('kg',0),'solid_present_kg':number('kg',0),'solid_returned_kg':number('kg',0),'solid_residual_kg':number('kg'),'gas_source_mol':number('mol',0),'gas_chamber_mol':number('mol',0),'gas_exhaust_mol':number('mol',0),'gas_residual_mol':number('mol'),'oil_reservoir_m3':number('m^3',0),'oil_pressurized_inventory_m3':number('m^3',0),'oil_residual_m3':number('m^3'),'hydraulic_stored_energy_j':number('J',0),'hydraulic_pump_work_j':number('J',0),'hydraulic_release_work_j':number('J',0),'capillary_work_j':number('J'),'work_balance_error_j':number('J')})
def interp(xs,ys,p):
if p<=xs[0]:return ys[0]
if p>=xs[-1]:return ys[-1]
i=bisect.bisect_right(xs,p)-1;return ys[i]+(ys[i+1]-ys[i])*(p-xs[i])/(xs[i+1]-xs[i])
def curve(ref,branch):
a={}
for p in LIB['substances'][ref]['value']:
if p['branch']==branch:a.setdefault(p['pressure_pa'],[]).append(p['volume_m3_kg'])
rows=sorted((p,sum(v)/len(v)) for p,v in a.items());blocks=[]
for p,v in rows:
blocks.append([max(v,0.),1])
while len(blocks)>1 and blocks[-2][0]/blocks[-2][1]>blocks[-1][0]/blocks[-1][1]:b=blocks.pop();blocks[-1][0]+=b[0];blocks[-1][1]+=b[1]
values=[s/n for s,n in blocks for _ in range(n)];return [p for p,v in rows],values
CURVES={(k,b):curve(k,b) for k in LIB['substances'] for b in ['intrusion','extrusion']}
def meta(ref):
d=LIB['substances'][ref];return dict(material_group=d['material_group'],material_class=d.get('material_class') or 'unspecified',pressure_axis=d.get('pressure_axis') or 'measured',volume_basis=d.get('volume_basis') or 'measured_cumulative',licence=d.get('licence') or d['source'].get('license') or 'see source')
MATERIAL_GROUPS=sorted({d['material_group'] for d in LIB['substances'].values()})
COUNT_NOTE=f"{len(LIB['substances'])}references/{len(MATERIAL_GROUPS)}materialgroups; specimens of one group are not independent materials; cross-instrument calibration transfer assumed"
def distribution(points):
a=[p for p in points if p['branch']=='intrusion' and p['diameter_m'] and p['pressure_pa']>0];a=sorted(a,key=lambda p:p['pressure_pa']);merged=[]
def resolution(p):return (.000763 if p['stage']=='low' else .0229 if p['pressure_pa']<=1500*PSI else .916)*PSI
for p in a:
if merged and p['pressure_pa']-merged[-1]['pressure_pa']<=.5*(resolution(p)+resolution(merged[-1])):
if resolution(p)<resolution(merged[-1]):merged[-1]=p
else:merged.append(p)
a=merged;d=[];v=[];dv=[]
for x,y in zip(a,a[1:]):
if y['diameter_m']>=x['diameter_m']:continue
diff=y['corrected_pore_volume_m3_kg']-x['corrected_pore_volume_m3_kg'];d.append(math.sqrt(x['diameter_m']*y['diameter_m']));v.append(diff);dv.append(diff/math.log10(x['diameter_m']/y['diameter_m']))
return dict(diameter_m=d,incremental_volume_m3_kg=v,differential_log_volume_m3_kg=dv,status='apparent_connected_throat_Washburn' if d else 'insufficient_points')
CAPS={};SLOTS={};SLOT_ZH={}
def cap(k,i,o,c,z,kind='device_command',vis='agent',ex=None,effects=None):CAPS[k]=(i,o,c,z,kind,vis,ex or {},effects or [])
def slot(k,s,u,z,o='derived',v='agent',c='controller',w=None):SLOTS[k]=(s,u,o,v,[c],w);SLOT_ZH[k]=z
cap('plant.configure',PLANT,obj({'configured':BOOL}),['controller','oil_pump'],'宿主选择有限气源、液压系统、响应及传感器假设','configuration','evaluator',PLANT_EXAMPLE,['plant.configured'])
cap('cell.configure',obj({'bulb_volume_m3':dict(number('m^3'),enum=[3.2e-6,6.6e-6,18e-6]),'stem_capacity_m3':dict(number('m^3'),enum=[.5e-6,2e-6])}),obj({'configured':BOOL}),['cell_z','cell_stem'],'选择原厂样品球泡及计量毛细管容量;几何固定3.2cc示意','configuration',ex={'bulb_volume_m3':3.2e-6,'stem_capacity_m3':.5e-6})
cap('sample.load',SAMPLE,obj({'loaded':BOOL}),['cell_z','sample_solid'],'宿主装入有限干固体,明确曲线跨仪器迁移','configuration','evaluator',SAMPLE_EXAMPLE)
cap('sample.unload',obj({}),obj({'returned_dry_mass_kg':number('kg',0),'retained_hg_kg':number('kg',0)}),['cell_z','sample_solid'],'自由汞排出后取回干样和滞留汞,保留耗材账本',vis='evaluator')
cap('mercury.fill',obj({'mass_kg':number('kg',1e-5,1)}),obj({'stock_kg':number('kg',0)}),['hg_reservoir'],'宿主加入有限汞库存,压入液不凭空生成','configuration','evaluator',{'mass_kg':.1})
cap('cell.drain',obj({}),obj({'waste_hg_kg':number('kg',0)}),['cell_z','hg_reservoir'],'卸压低压位人工排出自由汞;孔内滞留汞随样品返回',vis='evaluator')
cap('power.set',obj({'enabled':BOOL}),obj({'enabled':BOOL}),['power_switch','status_lamp'],'开关电源;断电保留压力和耗材,后续step卸压',ex={'enabled':True},effects=['power.enabled','power.angle_rad','lamp.power'])
for i in range(2):cap('guard'+str(i)+'.set',obj({'angle_rad':number('rad',0,1.4)}),obj({'angle_rad':number('rad',0,1.4)}),['guard'+str(i)],'低压位蓝罩人工开合;压力和运行互锁',ex={'angle_rad':0.},effects=['guard'+str(i)+'.angle_rad'])
cap('cap.set',obj({'lift_m':number('m',0,.19)}),obj({'lift_m':number('m',0,.19)}),['hp_cap'],'标准型手动高压盖拆装,非GT自动气动升降',ex={'lift_m':0.},effects=['cap.lift_m'])
cap('cell.transfer',obj({'destination':enum(['low0','low1','high'])}),obj({'position':TEXT}),['cell_x','cell_y','cell_z'],'受检人工转移同一有限样品管;两低压位可选,一高压位',vis='evaluator',ex={'destination':'high'},effects=['cell.x_m','cell.y_m','cell.z_m','cell.position'])
cap('method.configure',METHOD,obj({'configured':BOOL}),['controller'],'低高压分阶段扫描、平衡、输入质量、空隙闭合修正和Washburn参数','configuration',ex=METHOD_EXAMPLE)
cap('pressure.calibrate',PCAL,obj({'calibrated':BOOL}),['pressure_sensor_0','pressure_sensor_1','pressure_sensor_2'],'独立外部两点压力标定,三量程分别标定','configuration',ex=PCAL_EXAMPLE)
cap('volume.calibrate',VCAL,obj({'factor_m3_f':number('m^3/F',0),'zero_f':number('F')}),['cell_contact','controller'],'用独立外部已知体积和电容反演仪器体积标定','configuration',ex=VCAL_EXAMPLE)
cap('blank.calibrate',BLANK,obj({'points':INT(2,100000)}),['cell_stem','controller'],'保存空池/汞压缩/玻璃形变的外部实测或明确工程空白','configuration',ex={'pressures_pa':[0.,P_MAX],'volumes_m3':[0.,0.]})
cap('acquisition.start',obj({}),obj({'operation_id':TEXT,'phase':PHASE}),['controller','lp_manifold_0','lp_manifold_1','hp_vessel'],'低压抽空充汞或高压有限泵送,升降压测量,结束自动卸压',effects=['acquisition.phase','acquisition.stage'])
cap('acquisition.stop',obj({}),obj({'phase':PHASE}),['controller'],'取消保留压力与全部物质,step继续卸压',effects=['acquisition.phase'])
cap('emergency.stop',obj({}),obj({'phase':PHASE}),['front_estop'],'紧急停止升压;有限卸压需要后续仿真时钟',effects=['acquisition.phase'])
cap('process.measure',obj({}),RESULT,['controller'],'只读累计压入/退出点、孔容和孔喉分布','query')
cap('ledger.read',obj({}),LEDGER,['controller'],'有限汞/样品/N2/油及限定机械功账本','query','evaluator')
cap('template.reference',obj({'substance_id':TEXT}),obj({'name':TEXT,'evidence':TEXT,'source':TEXT,'intrusion_points':INT(0,100000),'extrusion_points':INT(0,100000),'material_group':TEXT,'material_class':TEXT,'pressure_axis':TEXT,'volume_basis':TEXT,'licence':TEXT}),['controller'],'参考曲线原始证据、材料组、压力轴/体积来源、许可和分支计数','query',ex={'substance_id':SID})
UNSUPPORTED={'hardware.connect','fault.probability_model','robot.load','low.dual_parallel','analysis.permeability','analysis.true_pore_network','coldtrap.vapour_model'}
for k in sorted(UNSUPPORTED):cap(k,obj({}),obj({}),['controller'],'未实现;不生成伪数据')
slot('plant.configured',BOOL,'1','宿主模型已配置','setpoint');slot('power.enabled',BOOL,'1','电源开关','setpoint',w=('power.set','enabled'));slot('power.angle_rad',number('rad',0,.32),'rad','前部电源摇臂位置','scene',c='power_switch');slot('lamp.power',BOOL,'1','前部电源灯','derived',c='status_lamp')
for i in range(2):slot('guard'+str(i)+'.angle_rad',number('rad',0,1.4),'rad','低压保护罩转角','scene',c='guard'+str(i),w=('guard'+str(i)+'.set','angle_rad'))
slot('cap.lift_m',number('m',0,.19),'m','手动高压盖移开高度','scene',c='hp_cap',w=('cap.set','lift_m'))
for a,h in [('x',.328),('y',.185),('z',.265)]:slot('cell.'+a+'_m',number('m',0,h),'m','同一玻璃管人工移位'+a,'scene',c='cell_'+a)
for k,s,u,z in [('position',TEXT,'1','玻璃管所处分析位'),('filled',BOOL,'1','样品管已充汞'),('loaded',BOOL,'1','样品管已装入固体')]:slot('cell.'+k,s,u,z,c='cell_z')
for k,s,u,z in [('phase',PHASE,'1','当前异步操作状态'),('stage',TEXT,'1','抽空/填充/压力平衡/卸压阶段'),('elapsed_s',number('s',0),'s','异步操作耗时'),('failure',TEXT,'1','运行失败原因')]:slot('acquisition.'+k,s,u,z)
slot('pressure.target_pa',number('Pa',0,P_MAX),'Pa','设定压力','setpoint');slot('pressure.measured_pa',number('Pa',0),'Pa','当前量程标定压力读数','sensor');slot('volume.measured_m3',nullable(number('m^3')),'m^3','独立电容标定和空白校正后的体积','sensor');slot('capacitance.measured_f',number('F'),'F','电容读数代理','sensor',c='cell_contact');slot('sample.identity',TEXT,'1','样品私有身份','process_truth','evaluator','sample_solid');slot('sample.mass_kg',number('kg',0),'kg','真实干质量','process_truth','evaluator','sample_solid');slot('sample.intruded_m3',number('m^3',0),'m^3','真实汞侵入量','process_truth','evaluator','sample_solid');slot('sample.pressure_pa',number('Pa',0),'Pa','真实毛细管驱动绝压','process_truth','evaluator');slot('results.point_count',INT(0,100000),'1','当前已完成的测量点数');slot('mercury.stock_kg',number('kg',0),'kg','汞库存余量','sensor',c='hg_reservoir')
# Public observable changes from synchronous commands, including derived sensor values.
# Conditional effects are listed even when a particular invocation leaves that value unchanged.
IMMEDIATE_EFFECTS={
'plant.configure':['plant.configured','pressure.measured_pa','capacitance.measured_f'],
'cell.configure':['volume.measured_m3'],
'sample.load':['cell.loaded','sample.identity','sample.mass_kg','sample.intruded_m3','results.point_count'],
'sample.unload':['cell.loaded','sample.identity','sample.mass_kg','sample.intruded_m3','capacitance.measured_f','volume.measured_m3'],
'mercury.fill':['mercury.stock_kg'],
'cell.drain':['cell.filled','capacitance.measured_f','volume.measured_m3'],
'power.set':['power.enabled','power.angle_rad','lamp.power','acquisition.phase','acquisition.stage','pressure.target_pa'],
'cell.transfer':['cell.x_m','cell.y_m','cell.z_m','cell.position','acquisition.stage','pressure.target_pa','sample.pressure_pa','pressure.measured_pa','capacitance.measured_f','volume.measured_m3'],
'pressure.calibrate':['pressure.measured_pa','volume.measured_m3'],
'volume.calibrate':['volume.measured_m3'],
'blank.calibrate':['volume.measured_m3'],
'acquisition.start':['acquisition.phase','acquisition.stage','acquisition.elapsed_s','acquisition.failure','pressure.target_pa'],
'acquisition.stop':['acquisition.phase','acquisition.stage','pressure.target_pa'],
'emergency.stop':['acquisition.phase','acquisition.stage','pressure.target_pa'],
}
STEP_EFFECTS=['pressure.target_pa','pressure.measured_pa','volume.measured_m3','capacitance.measured_f','sample.pressure_pa','sample.intruded_m3','mercury.stock_kg','cell.filled','acquisition.elapsed_s','acquisition.phase','acquisition.stage','acquisition.failure','results.point_count']
class AntonpaarPoremaster60Runtime:
def __init__(self,instance_id='poremaster60_01'):
self.instance_id=instance_id;self.time_s=0.;self.pending=0.;self.revision=0;self.plant=None;self.powered=False;self.guard=[0.,0.];self.cap=0.;self.position='low0';self.xyz=[0.,0.,0.];self.bulb=3.2e-6;self.capacity=.5e-6;self.sample=None;self.filled=False;self.hg_added=0.;self.hg_stock=0.;self.hg_cell=0.;self.hg_waste=0.;self.hg_returned=0.;self.v=0.;self.loaded=0.;self.returned=0.;self.gas=0.;self.source=0.;self.gas_initial=0.;self.exhaust=0.;self.oil=0.;self.oil_x=0.;self.p=AMBIENT;self.target=AMBIENT;self.peak=0.;self.pcal=[None]*3;self.vcal=None;self.blank=None;self.method=None;self.phase='idle';self.stage='idle';self.failure='';self.elapsed=0.;self.index=0;self.stable=0.;self.point_time=0.;self.points=[];self.all_points=[];self.serial=0;self.operation_id=None;self.records={};self._principals={};self._owners={};self._requests={};self.pump_work=0.;self.release_work=0.;self.capillary_work=0.;self.work_error=0.;self.branch='intrusion';self.result_source=''
def register_principal(self,principal_id,visibility='agent'):
if visibility not in ['agent','debug','evaluator'] or principal_id in self._principals:raise ActionRejected('REQUEST_CONFLICT')
self._principals[principal_id]=visibility
def session(self,principal_id):
if principal_id not in self._principals:raise ActionRejected('ACCESS_DENIED')
return AntonpaarPoremaster60Session(self,principal_id)
def describe(self):return export_antonpaar_poremaster60_contract_metadata()
def range_index(self):return 0 if self.position!='high' else 1 if self.p<=1500*PSI else 2
def resolution(self):return [.000763,.0229,.916][self.range_index()]*PSI
def indicated(self):
if not self.plant:return self.p
i=self.range_index();v=self.p*self.plant['pressure_gain'][i]+self.plant['pressure_offset_pa'][i]
if self.pcal[i]:v=(v-self.pcal[i][1])/self.pcal[i][0]
return max(0.,round(v/self.resolution())*self.resolution())
def blank_truth(self,p):return self.hg_cell/self.plant['hg_density_kg_m3']*(1-math.exp(-p/self.plant['hg_bulk_modulus_pa']))+self.plant['glass_compliance_m3_pa']*p if self.plant and self.filled else 0.
def capacitance(self):return (self.v+self.blank_truth(self.p))/self.plant['capacitance_volume_factor_m3_f']+self.plant['capacitance_offset_f'] if self.plant else 0.
def measured(self):
if not self.vcal:return None
v=(self.capacitance()-self.vcal[1])*self.vcal[0];v-=interp(*self.blank,self.indicated()) if self.blank else 0.;res=3e-11 if self.capacity==.5e-6 else 9e-11;return round(v/res)*res
def storage(self,p):return self.plant['hp_dead_volume_m3']*(-math.expm1(-max(p-AMBIENT,0)/self.plant['oil_bulk_modulus_pa']))
def pressure_hp(self,x,v):
f=max(0.,x-v)/self.plant['hp_dead_volume_m3'];return AMBIENT-self.plant['oil_bulk_modulus_pa']*math.log1p(-min(f,.999999))
def energy(self):
if not self.plant or self.position!='high':return 0.
d=max(self.p-AMBIENT,0);z=d/self.plant['oil_bulk_modulus_pa'];return self.plant['hp_dead_volume_m3']*self.plant['oil_bulk_modulus_pa']*(1-(1+z)*math.exp(-z))
def equilibrium(self,p,branch=None):
if not self.sample or not self.filled:return self.v
branch=branch or self.branch;xs,ys=CURVES[(self.sample['reference_id'],branch)]
if not xs:return self.v
q=interp([0.]+xs,[0.]+ys,p)*self.sample['true_dry_mass_kg']
return max(self.v,q) if branch=='intrusion' else min(self.v,q)
def read(self,visibility='agent'):
d={'plant.configured':bool(self.plant),'power.enabled':self.powered,'power.angle_rad':.32 if self.powered else 0.,'lamp.power':self.powered,'guard0.angle_rad':self.guard[0],'guard1.angle_rad':self.guard[1],'cap.lift_m':self.cap,'cell.x_m':self.xyz[0],'cell.y_m':self.xyz[1],'cell.z_m':self.xyz[2],'cell.position':self.position,'cell.filled':self.filled,'cell.loaded':bool(self.sample),'acquisition.phase':self.phase,'acquisition.stage':self.stage,'acquisition.elapsed_s':self.elapsed,'acquisition.failure':self.failure,'pressure.target_pa':self.target,'pressure.measured_pa':self.indicated(),'volume.measured_m3':self.measured(),'capacitance.measured_f':self.capacitance(),'sample.identity':self.sample['sample_id'] if self.sample else '', 'sample.mass_kg':self.sample['true_dry_mass_kg'] if self.sample else 0.,'sample.intruded_m3':self.v,'sample.pressure_pa':self.p,'results.point_count':len(self.all_points),'mercury.stock_kg':self.hg_stock}
return copy.deepcopy({k:v for k,v in d.items() if visibility!='agent' or SLOTS[k][3]=='agent'})
def _result(self):
points=copy.deepcopy(self.all_points);return dict(template_source=self.result_source,evidence=(LIB['substances'][self.sample['reference_id']]['evidence'] if self.sample else 'measured_literature')+'_reference_with_explicit_engineering_transfer',phase=self.phase,stage=self.stage,elapsed_s=self.elapsed,points=points,distribution=distribution(points),max_pore_volume_m3_kg=max((x['corrected_pore_volume_m3_kg'] for x in points),default=None),warnings=['apparent_connected_throat_Washburn; heterogeneous samples and compressibility may bias PSD',COUNT_NOTE,'extrusion only where the source measured a descent branch; source-peak cycle required; other references never fabricate descent']+([f"reference pressure axis {meta(self.sample['reference_id'])['pressure_axis']}: Washburn inversion of source diameters with assumed gamma/theta, absolute pressure scale uncertain"] if self.sample and meta(self.sample['reference_id'])['pressure_axis']=='washburn_assumed_params' else [])+([f"reference volume basis {meta(self.sample['reference_id'])['volume_basis']}: derived from source data (see library processing)"] if self.sample and meta(self.sample['reference_id'])['volume_basis'] not in ('measured_cumulative',) else [])+['monotone projection and duplicate-pressure means for runtime only; rawdata immutable; no measured-target extrapolation','one movable sample, two selectable LPports and one HPport; no dual-LP simultaneous process','finite gas/Hg/oil; constantT and lumped ideal liquid compliance; whole heat/mercuryvapour/robot/seal/OEMnoise not_run'])
def _ledger(self):
m=self.sample['true_dry_mass_kg'] if self.sample else 0.;intr=self.v*self.plant['hg_density_kg_m3'] if self.plant else 0.
return dict(hg_added_kg=self.hg_added,hg_stock_kg=self.hg_stock,hg_free_in_cell_kg=max(0.,self.hg_cell-intr),hg_intruded_kg=intr,hg_waste_kg=self.hg_waste,hg_returned_with_sample_kg=self.hg_returned,hg_residual_kg=self.hg_added-self.hg_stock-self.hg_cell-self.hg_waste-self.hg_returned,solid_loaded_kg=self.loaded,solid_present_kg=m,solid_returned_kg=self.returned,solid_residual_kg=self.loaded-m-self.returned,gas_source_mol=self.source,gas_chamber_mol=self.gas,gas_exhaust_mol=self.exhaust,gas_residual_mol=self.gas_initial-self.source-self.gas-self.exhaust,oil_reservoir_m3=self.oil,oil_pressurized_inventory_m3=self.oil_x,oil_residual_m3=(self.plant['oil_volume_m3'] if self.plant else 0)-self.oil-self.oil_x,hydraulic_stored_energy_j=self.energy(),hydraulic_pump_work_j=self.pump_work,hydraulic_release_work_j=self.release_work,capillary_work_j=self.capillary_work,work_balance_error_j=self.work_error)
def invoke(self,k,**a):
if k not in CAPS:raise ActionRejected('UNKNOWN_CAPABILITY')
if k in UNSUPPORTED:raise ActionRejected('UNSUPPORTED')
validate(CAPS[k][0],a);before=copy.deepcopy(self.__dict__)
try:
r=self._invoke(k,a);validate(CAPS[k][1],r)
if CAPS[k][4] not in ['query','analysis']:self.revision+=1
return r
except Exception:self.__dict__.clear();self.__dict__.update(before);raise
def _invoke(self,k,a):
if k=='process.measure':return self._result()
if k=='ledger.read':return self._ledger()
if k=='template.reference':
d=LIB['substances'].get(a['substance_id'])
if not d:raise ActionRejected('UNKNOWN_REFERENCE')
return dict(name=d['name'],evidence=d['evidence'],source=d['source']['url'],intrusion_points=sum(p['branch']=='intrusion' for p in d['value']),extrusion_points=sum(p['branch']=='extrusion' for p in d['value']),**meta(a['substance_id']))
if k=='plant.configure':
if self.plant or self.powered or not a['accept_engineering_model']:raise ActionRejected('INITIALIZATION_ONLY')
self.plant=copy.deepcopy(a);self.gas=AMBIENT*a['chamber_volume_m3']/(R*a['temperature_k']);self.source=a['source_pressure_pa']*a['source_volume_m3']/(R*a['temperature_k']);self.gas_initial=self.gas+self.source;self.oil=a['oil_volume_m3'];return {'configured':True}
if k=='power.set':
self.powered=a['enabled']
if not self.powered and self.phase=='running':self._end('cancelled')
return a
if not self.plant:raise ActionRejected('NOT_CONFIGURED')
if k in ['acquisition.stop','emergency.stop']:
if self.phase!='running' and k=='acquisition.stop':raise ActionRejected('NOT_RUNNING')
if self.phase=='running':self._end('cancelled')
self.target=AMBIENT;return {'phase':self.phase}
if self.phase=='running':raise ActionRejected('BUSY')
if k.startswith('guard'):
i=int(k[5]);v=a['angle_rad']
if abs(self.p-AMBIENT)>30:raise ActionRejected('PRESSURE_ACCESS_INTERLOCK')
self.guard[i]=v;return a
if k=='cap.set':
if abs(self.p-AMBIENT)>30:raise ActionRejected('PRESSURE_ACCESS_INTERLOCK')
self.cap=a['lift_m'];return a
if k=='cell.configure':
if self.sample or self.hg_cell:raise ActionRejected('LOAD_PRECONDITION')
self.bulb=float(a['bulb_volume_m3']);self.capacity=float(a['stem_capacity_m3']);return {'configured':True}
if k=='mercury.fill':self.hg_stock+=a['mass_kg'];self.hg_added+=a['mass_kg'];return {'stock_kg':self.hg_stock}
if k=='sample.load':
if self.sample or self.hg_cell or self.position=='high' or self.guard[int(self.position[-1])]<1.2 or abs(self.p-AMBIENT)>30:raise ActionRejected('LOAD_PRECONDITION')
if not a['dry'] or not a['accept_cross_instrument_transfer']:raise ActionRejected('TRANSFER_NOT_ACCEPTED')
if a['reference_id'] not in LIB['substances']:raise ActionRejected('UNKNOWN_REFERENCE')
if a['true_bulk_volume_m3']>=self.bulb or max(CURVES[(a['reference_id'],'intrusion')][1])*a['true_dry_mass_kg']>min(self.capacity,a['true_bulk_volume_m3']):raise ActionRejected('CAPACITY')
self.sample=copy.deepcopy(a);self.result_source=LIB['substances'][a['reference_id']]['source']['url'];self.v=0.;self.peak=0.;self.loaded+=a['true_dry_mass_kg'];self.all_points=[];return {'loaded':True}
if k=='sample.unload':
if not self.sample or self.position=='high' or self.guard[int(self.position[-1])]<1.2 or self.filled or abs(self.p-AMBIENT)>30:raise ActionRejected('LOAD_PRECONDITION')
m=self.sample['true_dry_mass_kg'];hg=self.hg_cell;self.returned+=m;self.hg_returned+=hg;self.hg_cell=0.;self.v=0.;self.sample=None;self.method=None;return dict(returned_dry_mass_kg=m,retained_hg_kg=hg)
if k=='cell.drain':
if self.position=='high' or abs(self.p-AMBIENT)>30 or self.guard[int(self.position[-1])]<1.2 or not self.filled:raise ActionRejected('LOAD_PRECONDITION')
keep=self.v*self.plant['hg_density_kg_m3'];self.hg_waste+=max(0.,self.hg_cell-keep);self.hg_cell=keep;self.filled=False;return {'waste_hg_kg':self.hg_waste}
if k=='cell.transfer':
dest=a['destination']
if abs(self.p-AMBIENT)>30 or not self.sample or dest==self.position:raise ActionRejected('TRANSFER_INTERLOCK')
for pos in [self.position,dest]:
if pos.startswith('low') and self.guard[int(pos[-1])]<1.2:raise ActionRejected('TRANSFER_INTERLOCK')
if 'high' in [self.position,dest] and self.cap<.18:raise ActionRejected('TRANSFER_INTERLOCK')
if dest=='high':
if not self.filled or not self.all_points:raise ActionRejected('LOW_STAGE_REQUIRED')
if self.oil<self.v:raise ActionRejected('OIL_EXHAUSTED')
self.oil-=self.v;self.oil_x=self.v
elif self.position=='high':self.oil+=self.oil_x;self.oil_x=0.
self.position=dest;self.xyz={'low0':[0.,0.,0.],'low1':[.328,0.,0.],'high':[.164,.185,.265]}[dest];self.method=None
if dest!='high':
self.p=self.gas*R*self.plant['temperature_k']/(self.plant['chamber_volume_m3']+self.v)
if abs(self.p-AMBIENT)>1:self.stage='vent';self.target=AMBIENT
return {'position':dest}
if k=='pressure.calibrate':
x=a['reference_pa'];y=a['measured_pa']
if x[1]<=x[0] or y[1]<=y[0]:raise ActionRejected('INVALID_CALIBRATION')
gain=(y[1]-y[0])/(x[1]-x[0]);self.pcal[a['range_index']]=(gain,y[0]-gain*x[0]);return {'calibrated':True}
if k=='volume.calibrate':
x=a['reference_volume_m3'];y=a['measured_capacitance_f']
if x[1]<=x[0] or y[1]<=y[0]:raise ActionRejected('INVALID_CALIBRATION')
factor=(x[1]-x[0])/(y[1]-y[0]);zero=y[0]-x[0]/factor;self.vcal=(factor,zero);return dict(factor_m3_f=factor,zero_f=zero)
if k=='blank.calibrate':
xs=a['pressures_pa'];ys=a['volumes_m3']
if len(xs)<2 or len(xs)!=len(ys) or any(b<=a for a,b in zip(xs,xs[1:])):raise ActionRejected('INVALID_CALIBRATION')
self.blank=(xs.copy(),ys.copy());return {'points':len(xs)}
if k=='method.configure':
xs=a['pressures_pa'];high=a['stage']=='high';lo,hi=(20*PSI,P_MAX) if high else (.2*PSI,50*PSI)
if not xs or len(xs)>2000 or any(not lo<=p<=hi for p in xs) or any(x==y for x,y in zip(xs,xs[1:])):raise ActionRejected('INVALID_PRESSURE_SEQUENCE')
peak=xs.index(max(xs))
if any(y<x for x,y in zip(xs[:peak+1],xs[1:peak+1])) or any(y>x for x,y in zip(xs[peak:],xs[peak+1:])):raise ActionRejected('INVALID_PRESSURE_SEQUENCE')
if not self.sample:raise ActionRejected('NOT_READY')
for i,p in enumerate(xs):
branch='intrusion' if i<=peak else 'extrusion';xp,_=CURVES[(self.sample['reference_id'],branch)]
if not xp:raise ActionRejected('EXTRUSION_UNAVAILABLE')
if p<xp[0]*(1-1e-5) or p>xp[-1]*(1+1e-5):raise ActionRejected('TEMPLATE_RANGE')
if peak<len(xs)-1:
xp,_=CURVES[(self.sample['reference_id'],'extrusion')]
if abs(max(xs)-max(xp))/max(xp)>.0001:raise ActionRejected('SOURCE_PEAK_REQUIRED')
if a['pressure_tolerance_pa']<( .916*PSI if high and max(xs)>1500*PSI else .0229*PSI if high else .000763*PSI)/2:raise ActionRejected('BELOW_RESOLUTION')
self.method=copy.deepcopy(a);return {'configured':True}
if k=='acquisition.start':
if self.stage=='vent' or abs(self.p-AMBIENT)>30 or not self.powered or not self.sample or not self.method or not self.vcal or not self.blank:raise ActionRejected('NOT_READY')
high=self.method['stage']=='high'
if high!=(self.position=='high') or high and self.cap>.0001 or not high and self.guard[int(self.position[-1])]>.0001:raise ActionRejected('POSITION_INTERLOCK')
if (high and any(x is None for x in self.pcal[1:])) or (not high and self.pcal[0] is None):raise ActionRejected('CALIBRATION_REQUIRED')
if not high and self.filled:raise ActionRejected('FRESH_LOW_STAGE_REQUIRED')
if high and not self.filled:raise ActionRejected('LOW_STAGE_REQUIRED')
xs=self.method['pressures_pa']
if self.blank[0][0]>min(xs) or self.blank[0][-1]<max(xs):raise ActionRejected('BLANK_RANGE')
if self.operation_id and self.operation_id not in self.records:self.records[self.operation_id]=self._result()
self.serial+=1;self.operation_id=self.instance_id+':micp:'+str(self.serial);self.phase='running';self.stage='pressure' if high else 'vacuum';self.elapsed=0.;self.stable=0.;self.index=0;self.point_time=0.;self.points=[];self.failure='';self.target=xs[0] if high else 3.333;self.branch='intrusion';return {'operation_id':self.operation_id,'phase':self.phase}
raise ActionRejected('UNKNOWN_CAPABILITY')
def _end(self,phase,reason=''):
self.phase=phase;self.failure=reason;self.stage='vent';self.target=AMBIENT
if self.operation_id:self.records[self.operation_id]=self._result()
def step(self,dt):
if isinstance(dt,bool) or not isinstance(dt,(int,float)) or not math.isfinite(dt) or dt<0 or dt>86400:raise ActionRejected('INVALID_ARGUMENT')
self.pending+=dt
while self.pending+1e-10>=DT:
self.pending-=DT;self.time_s+=DT;self._tick();self.revision+=1
if abs(self.pending)<1e-10:self.pending=0.
def _tick(self):
if not self.plant:return
running=self.phase=='running';oldp=self.p;oldv=self.v;P=self.plant
if running:self.elapsed+=DT;self.point_time+=DT
if self.stage=='vacuum' and running:
dn=self.gas*(-math.expm1(-P['pump_rate_s']*DT));self.gas-=dn;self.exhaust+=dn;self.p=self.gas*R*P['temperature_k']/P['chamber_volume_m3']
if self.p<=3.333:self.stage='fill';self.target=self.p
elif self.stage=='fill' and running:
desired=(self.bulb-self.sample['true_bulk_volume_m3']+self.capacity)*P['hg_density_kg_m3'];dm=min(.01*DT,max(0.,desired-self.hg_cell),self.hg_stock);self.hg_cell+=dm;self.hg_stock-=dm
if desired-self.hg_cell<1e-12:self.filled=True;self.stage='pressure';self.target=self.method['pressures_pa'][0];self.point_time=0.
elif self.hg_stock<1e-12:self._end('failed','MERCURY_EXHAUSTED')
elif self.stage in ['pressure','vent']:
vent=self.stage=='vent';target=AMBIENT if vent else self.method['pressures_pa'][self.index];self.target=target;rate=(2e8 if self.position=='high' else 5e5) if vent else self.method['pressure_rate_pa_s'];ramped=self.p+max(-rate*DT,min(rate*DT,target-self.p));a=-math.expm1(-P['intrusion_rate_s']*DT)
# After scan ends, retained Hg is held; no unsupported extrusion is invented during vent.
branch=self.branch;vnew=self.v if vent else self.v+a*(self.equilibrium(ramped,branch)-self.v)
if vnew>self.capacity+1e-14 or vnew*P['hg_density_kg_m3']>self.hg_cell+1e-12:self._end('failed','MERCURY_OR_STEM_CAPACITY');return
if self.position=='high':
desired=self.storage(ramped)+vnew;dx=max(-P['oil_flow_m3_s']*DT,min(P['oil_flow_m3_s']*DT,desired-self.oil_x));dx=min(dx,self.oil);x=self.oil_x+dx
vnew=min(vnew,x);self.oil-=dx;self.oil_x=x;self.v=max(0.,vnew);self.p=self.pressure_hp(x,self.v);pavg=(max(oldp-AMBIENT,0)+max(self.p-AMBIENT,0))/2;dw=pavg*dx;dc=pavg*(self.v-oldv)
if dw>=0:self.pump_work+=dw
else:self.release_work-=dw
self.capillary_work+=dc;self.work_error=self.pump_work-self.release_work-self.capillary_work-self.energy()
if not vent and self.oil<1e-14 and target>self.p+100:self._end('failed','OIL_EXHAUSTED')
else:
self.v=max(0.,vnew);V=P['chamber_volume_m3']+self.v;desired=ramped*V/(R*P['temperature_k']);dn=(desired-self.gas)*(-math.expm1(-P['gas_rate_s']*DT))
if dn>=0:
ps=self.source*R*P['temperature_k']/P['source_volume_m3'];equal=max(0.,(ps-self.p)/(R*P['temperature_k']*(1/P['source_volume_m3']+1/V)));dn=min(dn,self.source,equal);self.source-=dn
else:self.exhaust-=dn
self.gas+=dn;self.p=self.gas*R*P['temperature_k']/V
if not vent and self.source*R*P['temperature_k']/P['source_volume_m3']<target and abs(self.p-target)>100:self._end('failed','GAS_EXHAUSTED')
self.peak=max(self.peak,self.p)
if self.p>P_MAX*1.001:self._end('failed','OVERPRESSURE')
if vent:
if abs(self.p-AMBIENT)<1.:
if self.phase=='running':self.phase='succeeded'
self.stage='idle';self.target=AMBIENT
if self.phase=='succeeded' and self.operation_id:self.records[self.operation_id]=self._result()
else:
okay=abs(self.indicated()-target)<=self.method['pressure_tolerance_pa'] and abs(self.v-oldv)/DT<=self.method['max_volume_drift_m3_s'];self.stable=self.stable+DT if okay else 0.
if self.stable+1e-9>=self.method['equilibration_s']:
p=self.indicated();v=self.measured();q=v/self.method['entered_mass_kg'];angle=self.method['advancing_angle_rad' if self.branch=='intrusion' else 'receding_angle_rad'];d=-4*self.method['surface_tension_n_m']*math.cos(angle)/p if p>0 else None;point=dict(time_s=self.time_s,stage=self.method['stage'],branch=self.branch,pressure_pa=p,intrusion_volume_m3=v,specific_volume_m3_kg=q,corrected_pore_volume_m3_kg=max(0.,q-self.method['closure_m3_kg']),diameter_m=d);self.points.append(point);self.all_points.append(point);self.index+=1;self.stable=0.;self.point_time=0.
if self.index==len(self.method['pressures_pa']):self.stage='vent';self.target=AMBIENT
elif self.method['pressures_pa'][self.index]<self.method['pressures_pa'][self.index-1]:self.branch='extrusion'
if self.phase=='running' and self.point_time>self.method['point_timeout_s']:self._end('failed','POINT_TIMEOUT')
class AntonpaarPoremaster60Session:
def __init__(self,host,principal_id):self._host=host;self._principal=principal_id
@property
def _role(self):return self._host._principals[self._principal]
def _target(self,i):
if i!=self._host.instance_id:raise ActionRejected('UNKNOWN_INSTANCE')
def describe(self,*,instance_id=None,asset_type_id=None):
if (instance_id is None)==(asset_type_id is None):raise ActionRejected('INVALID_ARGUMENT')
if instance_id is not None:self._target(instance_id)
if asset_type_id is not None and asset_type_id!=ASSET_TYPE_ID:raise ActionRejected('UNKNOWN_INSTANCE')
m=export_antonpaar_poremaster60_contract_metadata();return dict(protocol_version=PROTOCOL_VERSION,asset_type_id=ASSET_TYPE_ID,asset_version='1.0.0',capabilities={k:v for k,v in m['capabilities'].items() if v['visibility']=='agent' or self._role!='agent'},state_slots={k:v for k,v in m['state_slots'].items() if v['visibility']=='agent' or self._role!='agent'})
def read(self,*,instance_id,state_ids=None):
self._target(instance_id);h=self._host;v=h.read(self._role);ids=list(v) if state_ids is None else state_ids
if not isinstance(ids,list) or any(not isinstance(k,str) for k in ids):raise ActionRejected('INVALID_ARGUMENT')
if any(k not in v for k in ids):raise ActionRejected('ACCESS_DENIED')
return dict(status='succeeded',instance_id=instance_id,state_revision=h.revision,clock={'domain':'simulation','time_s':h.time_s},observations={k:dict(value=v[k],unit=SLOTS[k][1],quality='unavailable' if v[k] is None else 'estimated' if SLOTS[k][2]=='derived' else 'valid',sample_time_s=h.time_s,sample_window_s=None) for k in ids})
def invoke(self,*,instance_id,capability_id,arguments,request_id):
h=self._host
try:
self._target(instance_id)
if not isinstance(capability_id,str) or capability_id not in CAPS:raise ActionRejected('UNKNOWN_CAPABILITY')
if self._role=='agent' and CAPS[capability_id][5]!='agent':raise ActionRejected('ACCESS_DENIED')
if not isinstance(request_id,str) or not request_id:raise ActionRejected('INVALID_ARGUMENT')
validate(CAPS[capability_id][0],arguments);key=(self._principal,instance_id,request_id);digest=json.dumps([capability_id,arguments],sort_keys=True,allow_nan=False)
if key in h._requests:
old,result=h._requests[key]
if old!=digest:raise ActionRejected('REQUEST_CONFLICT')
return copy.deepcopy(result)
result=h.invoke(capability_id,**arguments);op=result.get('operation_id')
if op:h._owners[op]=self._principal
response=dict(protocol_version=PROTOCOL_VERSION,instance_id=instance_id,request_id=request_id,operation_id=op,status='accepted' if op else 'succeeded',state_revision=h.revision,clock={'domain':'simulation','time_s':h.time_s},result=result,observations={},error=None);h._requests[key]=(digest,copy.deepcopy(response));return response
except ActionRejected as exc:return dict(protocol_version=PROTOCOL_VERSION,instance_id=instance_id,request_id=request_id,operation_id=None,status='unsupported' if str(exc)=='UNSUPPORTED' else 'rejected',state_revision=h.revision,clock={'domain':'simulation','time_s':h.time_s},result={},observations={},error=dict(code=str(exc),message=str(exc),retryable=False,side_effects='none'))
def write(self,*,instance_id,state_id,value,request_id):
self._target(instance_id)
if state_id not in SLOTS or not SLOTS[state_id][5]:raise ActionRejected('ACCESS_DENIED')
cap,arg=SLOTS[state_id][5];return self.invoke(instance_id=instance_id,capability_id=cap,arguments={arg:value},request_id=request_id)
def poll(self,operation_id):
h=self._host
if h._owners.get(operation_id)!=self._principal:raise ActionRejected('ACCESS_DENIED')
record=h.records.get(operation_id)
if operation_id==h.operation_id and h.phase=='running':record=h._result()
if record is None:raise ActionRejected('UNKNOWN_OPERATION')
return dict(operation_id=operation_id,status=record['phase'],result=copy.deepcopy(record))
def cancel(self,operation_id,request_id):
self.poll(operation_id)
if operation_id!=self._host.operation_id:raise ActionRejected('NOT_RUNNING')
return self.invoke(instance_id=self._host.instance_id,capability_id='acquisition.stop',arguments={},request_id=request_id)
def export_antonpaar_poremaster60_contract_metadata():
caps={};slots={}
for k,(s,u,o,v,c,w) in SLOTS.items():slots[k]=dict(meaning_zh=SLOT_ZH[k],component_ids=c,value_schema=copy.deepcopy(s),unit=u,reference_conditions='SI; absolute pressure axis per original PoreMaster brochure; constant externally supplied temperature; actual sample identity private',origin=o,visibility=v,access='read_write' if w else 'read_only',read_binding=dict(backend='host',artifact_id='runtime',accessor=f'AntonpaarPoremaster60Session.read(state_ids=[{k!r}])'),write_via=dict(capability_id=w[0],argument=w[1],fixed_arguments={}) if w else None,sampling=dict(mode='instant',time_domain='simulation',window_description='fixed0.1s integration; pure reads never advance'),source_ids=['simulation_assumption'])
errors=['INVALID_ARGUMENT','UNKNOWN_INSTANCE','UNKNOWN_CAPABILITY','UNKNOWN_OPERATION','UNSUPPORTED','ACCESS_DENIED','REQUEST_CONFLICT','INITIALIZATION_ONLY','BUSY','NOT_READY','NOT_RUNNING','NOT_CONFIGURED','UNKNOWN_REFERENCE','PRESSURE_ACCESS_INTERLOCK','LOAD_PRECONDITION','TRANSFER_INTERLOCK','TRANSFER_NOT_ACCEPTED','CAPACITY','OIL_EXHAUSTED','GAS_EXHAUSTED','MERCURY_EXHAUSTED','MERCURY_OR_STEM_CAPACITY','POSITION_INTERLOCK','LOW_STAGE_REQUIRED','INVALID_PRESSURE_SEQUENCE','INVALID_CALIBRATION','EXTRUSION_UNAVAILABLE','SOURCE_PEAK_REQUIRED','TEMPLATE_RANGE','BELOW_RESOLUTION','CALIBRATION_REQUIRED','FRESH_LOW_STAGE_REQUIRED','BLANK_RANGE','OVERPRESSURE','POINT_TIMEOUT']
for k,(inp,out,c,z,kind,vis,ex,effects) in CAPS.items():
un=k in UNSUPPORTED;asyn=k=='acquisition.start';caps[k]=dict(function_zh=z,kind=kind,visibility=vis,component_ids=c,availability='unsupported' if un else 'implemented',input_schema=copy.deepcopy(inp),output_schema=copy.deepcopy(out),implementation=dict(process='absent' if un else 'implemented',scene='absent',robot='absent',hardware='absent',host='absent' if un else 'implemented'),binding=None if un else dict(backend='host',artifact_id='runtime',entrypoint='asset_runtime.antonpaar_poremaster60.AntonpaarPoremaster60Session.invoke',invocation=f'session.invoke(instance_id="poremaster60_01",capability_id={k!r},arguments={ex!r},request_id="unique")'),preconditions=[] if kind in ['query','analysis'] or un else [dict(description_zh='有限干样/汞/气源/液压油;宿主接受响应迁移;独立标定;受检压力和机械访问',state_ids=['power.enabled','plant.configured','acquisition.phase','cell.position','cap.lift_m','guard0.angle_rad','guard1.angle_rad'],enforced_by='runtime',check='atomic invoke and host-authenticated Session; advance only step')],state_effects=[dict(state_id=x,timing='immediate',description_zh='经互锁检查更新状态') for x in IMMEDIATE_EFFECTS.get(k,effects)],observes=[],model_effects=dict(mode='none',description_zh='场景需独立验证',binding_ids=[]),execution=dict(mode='asynchronous' if asyn else 'synchronous',time_domain='simulation',completion_criterion='压力点完成且卸压接近环境绝压' if asyn else '命令接受,过程由step推进',completion_state_ids=['acquisition.phase'] if asyn else [],timeout_s=None,cancellation='supported' if asyn else 'unsupported',retry='same_request_id',resources=['host_clock','one_finite_sample','mercury','gas','hydraulic_oil','request_cache'],partial_failure_zh='已消耗的汞/气源/液压状态、已采点保留,取消不瞬间归零压力;之后step有限卸压'),errors=[dict(code=x,meaning_zh=x,side_effects='none') for x in errors],example_arguments=copy.deepcopy(ex),verification=[],limitations=['非厂家软件/实机协议;误差参数是独立宿主假设;分辨率不是噪声精度实证'],source_ids=['manufacturer_specs','simulation_assumption'])
if asyn:caps[k]['state_effects'] += [dict(state_id=x,timing='on_step',description_zh='有限汞/气源/液压油及压力平衡更新') for x in STEP_EFFECTS]
mech=dict(component_ids=['controller','oil_pump','hg_reservoir','lp_manifold_0','lp_manifold_1','hp_vessel','cell_z','cell_stem','cell_contact','coldtrap'],state_ids=list(slots),meaning_zh='分阶段有限汞压入、真实分支曲线迁移、独立压力/电容/空白标定和连通孔喉反演',implementation='lumped',equations=['Washburn D=-4*gamma*cos(theta)/P; gamma and advancing/receding angles are independently entered method conditions','Raw experimental q(P) retained in library; runtime duplicate-P means + isotonic projection + explicitly assumed zero-pressure bridge; measured targets reject out-of-support extrapolation','v_new=v+(1-exp(-k*dt))*(m_true*q_equilibrium(P)-v); intrusion monotone, extrusion only two measured hemp references at recorded source-peak cycle','LP P=nRT/(Vchamber+Vintruded); finite N2 source gradient/equalization cap; vacuum and vent book exhaust; constantT explicit','HP oil_compression=V0*(1-exp(-(P-Patm)/K)); oil_inventory=oil_compression+Vintruded; finite oil flow and reservoir; P=Patm-K*ln(1-(X-Vintruded)/V0)','Hg(stock)+Hg(cell free)+Hg(pore)+Hg(waste)+Hg(sample returned)=Hg externally added; solid loaded=present+returned','Capacitance=(Vintruded+Hgcompression+glassCompliance*P)/true_m3_per_F+offset_F; volume_calibrated=(C-zero_cal)*factor_cal-blank(Pmeasured); quantized3e-11m3(0.5cc) or9e-11m3(2cc)','Pressure indicated=quantize((gain*P+offset-cal_offset)/cal_gain,range_resolution); three calibration ranges separate','Reported specific volume=calibrated_volume/entered_mass; pore volume=max(0,specific_volume-entered_closure); never copy true mass into reported normalization','LP/HP overlap points within combined pressure quantization half-width are merged, keeping higher pressure resolution; dV/dlog10D only over distinguishable pressure intervals at geometric-mean diameter; source missing extrusion remains unavailable','Hydraulic stored gauge work=V0*K*(1-(1+z)*exp(-z)),z=(P-Patm)/K; trapezoidal pump/return/capillary work reports residual; excludes absolute ambient work, lowpressuregas thermal energy, heat and vapour'],parameters={},source_ids=['manufacturer_specs','manufacturer_brochure','dggs_micp','limestone_data','hemp_data','simulation_assumption'],limitations=[f"{len(LIB['substances'])} reference specimens in {len(MATERIAL_GROUPS)} distinct material groups (rocks, clays, cements/mortars/screeds, ceramics, membranes, polymer/carbon foams, glass, soil, plant fibre); source instruments AutoPore/WIN9400/Pascal/PoreSizer/unspecified, not PoreMaster60 reproducibility data; {sum(1 for d in LIB['substances'].values() if d.get('pressure_axis')=='washburn_assumed_params')} references have an assumption-flagged Washburn pressure axis.",f"{sum(1 for k in LIB['substances'] if not CURVES[(k,'extrusion')][0])} references lack extrusion; only the {sum(1 for k in LIB['substances'] if CURVES[(k,'extrusion')][0])} with a measured descent branch can run a cycle. Small loops, pore-network hysteresis and irreversible sample compression not validated.",'One movable physical cell, two selectable LPports and oneHP; parallel LP throughput unsupported. Semantic manual relocation verifies position, not robot trajectory/contact/sealing.','3.2/6.6/18cc bulb and0.5/2cc stem semantic choices; displayed glass is3.2cc proxy; exact bore CAD/part masses/inertia unknown.','Standard180kg historical manufacturer body; GT lift absent; current revision CAD unknown;1000VA not heat power.','Calibrations use externally supplied records; example blanks are explicitly engineering records, not empirical OEM blank validation.','Oil compliance and transfer rates engineering; constanttemperature, mercury vapour/coldtrap chemistry, gas/pump/sample/whole-machine enthalpy, OEMnoise/fault probability not_run.','Fixture pressure integrity, physical robot/grasp/contact, real hardware and filesystem truth isolation not_run.'])
spec=importlib.util.spec_from_file_location('_poremaster_annotations',ROOT/'scripts/asset_runtime/_annotations.py');ann=importlib.util.module_from_spec(spec);spec.loader.exec_module(ann);ann.KEY_ZH.update(SLOT_ZH);ann.TRUTH_ZH.update(SLOT_ZH);ann.annotate_export(SLUG,caps,slots,{'mercury_porosimetry':mech},inputs={'plant.configure':(PLANT,PLANT_EXAMPLE),'method.configure':(METHOD,METHOD_EXAMPLE),'sample.load':(SAMPLE,SAMPLE_EXAMPLE)})
for k,v in slots.items():v['meaning_zh']=SLOT_ZH[k]+';来源='+v['origin']+'。'
return dict(asset_type_id=ASSET_TYPE_ID,catalog_id=CATALOG_ID,capabilities=caps,state_slots=slots,mechanisms={'mercury_porosimetry':mech})
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