From a726d5d2ec7fe0c15a30cced3abf1b690c9f266d Mon Sep 17 00:00:00 2001 From: "pre-commit-ci-lite[bot]" <117423508+pre-commit-ci-lite[bot]@users.noreply.github.com> Date: Sun, 6 Oct 2024 13:45:54 +0000 Subject: [PATCH] [pre-commit.ci lite] apply automatic fixes --- tests/process/test_ProcessTools.py | 54 ++++++++++++++---------------- 1 file changed, 26 insertions(+), 28 deletions(-) diff --git a/tests/process/test_ProcessTools.py b/tests/process/test_ProcessTools.py index 746e9d1..777cbf0 100644 --- a/tests/process/test_ProcessTools.py +++ b/tests/process/test_ProcessTools.py @@ -35,8 +35,8 @@ def test_compsplitter(): fluid1.addComponent("CO2", 2.3, "mol/sec") fluid1.setMixingRule(2) clearProcess() - stream1 = stream('stream1', fluid1) - splittcomp = compsplitter('splitter 1', stream1, [1.0, 0.0]) + stream1 = stream("stream1", fluid1) + splittcomp = compsplitter("splitter 1", stream1, [1.0, 0.0]) runProcess() TPflash(splittcomp.getSplitStream(0).getFluid()) printFrame(splittcomp.getSplitStream(0).getFluid()) @@ -51,8 +51,8 @@ def test_waterDewPointAnalyser(): fluid1.addComponent("water", 50e-6, "mol/sec") fluid1.setMixingRule(2) clearProcess() - stream1 = stream('stream1', fluid1) - waterDewPoint = waterDewPointAnalyser('water', stream1) + stream1 = stream("stream1", fluid1) + waterDewPoint = waterDewPointAnalyser("water", stream1) runProcess() assert waterDewPoint.getMeasuredValue("C") == approx(-11.828217379989212, rel=0.001) @@ -68,8 +68,8 @@ def test_hydrateEquilibriumTemperatureAnalyser(): fluid1.addComponent("water", 50e-6, "mol/sec") fluid1.setMixingRule(2) clearProcess() - stream1 = stream('stream1', fluid1) - hydrateDewPoint = hydrateEquilibriumTemperatureAnalyser('analyser1', stream1) + stream1 = stream("stream1", fluid1) + hydrateDewPoint = hydrateEquilibriumTemperatureAnalyser("analyser1", stream1) runProcess() assert hydrateDewPoint.getMeasuredValue("C") == approx(-25.204324, rel=0.001) @@ -88,11 +88,11 @@ def test_runProcessAsThread(): fluid1.setMixingRule(2) clearProcess() stream1 = stream("stream1", fluid1) - waterDewPoint = waterDewPointAnalyser('analy', stream1) - stream2 = stream('stream2', fluid1) - waterDewPoint2 = waterDewPointAnalyser('anal1', stream2) - stream3 = stream('stream3', fluid1) - waterDewPoint3 = waterDewPointAnalyser('water2', stream3) + waterDewPoint = waterDewPointAnalyser("analy", stream1) + stream2 = stream("stream2", fluid1) + waterDewPoint2 = waterDewPointAnalyser("anal1", stream2) + stream3 = stream("stream3", fluid1) + waterDewPoint3 = waterDewPointAnalyser("water2", stream3) processThread = runProcessAsThread() # assert waterDewPoint2.getMeasuredValue('C') != approx(-11.828217379989212, rel= 0.001) processThread.join(10000) # max 10 sec calculation time @@ -108,12 +108,12 @@ def test_newprocess(): fluid1.addComponent("nitrogen", 1.0, "mol/sec") fluid1.addComponent("CO2", 2.3, "mol/sec") fluid1.setMixingRule(2) - stream1 = stream('str11', fluid1) - splittcomp = compsplitter('split1', stream1, [1.0, 0.0]) + stream1 = stream("str11", fluid1) + splittcomp = compsplitter("split1", stream1, [1.0, 0.0]) runProcess() newProcess() - stream1 = stream('str2', fluid1) - splittcomp = compsplitter('split2', stream1, [1.0, 0.0]) + stream1 = stream("str2", fluid1) + splittcomp = compsplitter("split2", stream1, [1.0, 0.0]) runProcess() TPflash(splittcomp.getSplitStream(0).getFluid()) # assert splittcomp.getSplitStream(0).getFluid().getViscosity('kg/msec') > 1e-19 @@ -130,21 +130,19 @@ def test_flowSplitter(): clearProcess() - stream1 = stream('str1', fluid1) + stream1 = stream("str1", fluid1) stream1.setPressure(pressure_inlet, "bara") stream1.setTemperature(temperature_inlet, "C") stream1.setFlowRate(gasFlowRate, "MSm3/day") - streamresycl = stream('str2', stream1.getFluid().clone()) + streamresycl = stream("str2", stream1.getFluid().clone()) streamresycl.setFlowRate(0.1, "MSm3/day") mixerStream = mixer("mixer1") mixerStream.addStream(stream1) mixerStream.addStream(streamresycl) - compressor_1 = compressor('comp1', - mixerStream.getOutletStream(), pressure_outlet - ) + compressor_1 = compressor("comp1", mixerStream.getOutletStream(), pressure_outlet) stream2 = stream("stre333", compressor_1.getOutStream()) @@ -187,9 +185,9 @@ def test_virtualstream(): fluid1.addComponent("methane", 1.0) clearProcess() - stream1 = stream('str1', fluid1) + stream1 = stream("str1", fluid1) stream1.setFlowRate(3.1, "MSm3/day") - vstream = virtualstream('str2', stream1) + vstream = virtualstream("str2", stream1) vstream.setFlowRate(1.1, "MSm3/day") vstream.setTemperature(25.0, "C") vstream.setPressure(25.0, "bara") @@ -355,7 +353,7 @@ def test_gasoilprocess(): clearProcess() # Well stream - wstream_inlet = stream('str11', WellFluid2) + wstream_inlet = stream("str11", WellFluid2) wstream_inlet.setTemperature(feedTemperature, "K") wstream_inlet.setPressure(feedPressure, "bara") wstream_inlet.setFlowRate(reffluidrate, "kg/hr") @@ -363,10 +361,10 @@ def test_gasoilprocess(): # Separator train separator1 = separator3phase("inlet separator", wstream_inlet) valve1 = valve("HP oil valve", separator1.getOilOutStream(), MPpressure) - Oilheater1 = heater('heater 2', valve1.getOutletStream()) + Oilheater1 = heater("heater 2", valve1.getOutletStream()) Oilheater1.setOutTemperature(359.15) separator2 = separator3phase("MP separator", Oilheater1.getOutStream()) - valve2 = valve('valv1', separator2.getOilOutStream(), LPpressure) + valve2 = valve("valv1", separator2.getOilOutStream(), LPpressure) recirc1stream = stream("str1", valve2.getOutletStream().clone()) recirc2stream = stream("str2", valve2.getOutletStream().clone()) recirc3stream = stream("str3", valve2.getOutletStream().clone()) @@ -407,12 +405,12 @@ def test_gasoilprocess(): # 3rd stg compressor, compressor model is skipped as the target for reference # model is to derive gas composition into 3rd stage and then perform more detailed # calculation on 3rd stage compressor - mixerMP = mixer('mix1') + mixerMP = mixer("mix1") mixerMP.addStream(compressorMP1.getOutStream()) mixerMP.addStream(separator2.getGasOutStream()) - cooler3rd = heater('he1', mixerMP.getOutStream()) + cooler3rd = heater("he1", mixerMP.getOutStream()) cooler3rd.setOutTemperature(317.15) - scrubber3rd = separator('ss1', cooler3rd.getOutStream()) + scrubber3rd = separator("ss1", cooler3rd.getOutStream()) # Recycle for liquid from 2nd stage scrubber valveR3 = valve("3re scr liq", scrubber3rd.getLiquidOutStream(), LPpressure)