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Overview

STREAMS1
UOPS1
THERM1
CONVERGE1
TOPOLOGY1

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Sheet 1: STREAMS1

CHEMCAD	6.1.4	Page	1
Job name:	przykład	Date:	2012-01-05	Time:	17:27:49
STREAM PROPERTIES
Stream No.	1	2	3	4	5	6	7	8	9
Name
- - Overall - -
Molar flow kmol/h	8,1689	8,1689	8,1689	5,2816	5,2816	2,0735	3,2081	0,3208	2,8873
Mass flow kg/h	100	100	100	100,0006	100,0006	4,1798	95,8208	9	86,8208
Temp K	298	567,2568	750	750	613,5513	298	298	298	298
Pres bar	1	10	10	10	1	1	1	1	1
Vapor mole fraction	1	1	1	1	1	1	1	1	1
Enth MJ/h	167,61	254,97	325,75	-84,979	-134,72	-0,0080855	-225,53	16,757	-242,29
Tc K	173,3344	173,3344	173,3344	242,6789	242,6789	33,27	303,38	282,41	305,43
Pc bar	74,9484	74,9484	74,9484	80,4645	80,4645	12,9595	49,2427	50,318	48,8386
Std. sp gr. wtr = 1	0,25	0,25	0,25	0,304	0,304	0,07	0,356	0,35	0,356
Std. sp gr. air = 1	0,423	0,423	0,423	0,654	0,654	0,07	1,031	0,969	1,038
Degree API	434,5	434,5	434,5	334,0756	334,0756	1889,9283	266,2077	272,7857	265,5258
Average mol wt	12,2415	12,2415	12,2415	18,9337	18,9337	2,0158	29,8684	28,054	30,07
Actual dens kg/m3	0,4945	2,5885	1,9571	3,028	0,3711	0,0813	1,2146	1,139	1,223
Actual vol m3/h	202,2273	38,632	51,0949	33,0255	269,4357	51,3948	78,8918	7,9018	70,9876
Std liq m3/h	0,4	0,4	0,4	0,329	0,329	0,0597	0,2693	0,0257	0,2436
Std vap 0 C m3/h	183,095	183,095	183,095	118,3804	118,3804	46,4752	71,9052	7,1905	64,7147
- - Vapor only - -
Molar flow kmol/h	8,1689	8,1689	8,1689	5,2816	5,2816	2,0735	3,2081	0,3208	2,8873
Mass flow kg/h	100	100	100	100,0006	100,0006	4,1798	95,8208	9	86,8208
Average mol wt	12,2415	12,2415	12,2415	18,9337	18,9337	2,0158	29,8684	28,054	30,07
Actual dens kg/m3	0,4945	2,5885	1,9571	3,028	0,3711	0,0813	1,2146	1,139	1,223
Actual vol m3/h	202,2273	38,632	51,0949	33,0255	269,4357	51,3948	78,8918	7,9018	70,9876
Std liq m3/h	0,4	0,4	0,4	0,329	0,329	0,0597	0,2693	0,0257	0,2436
Std vap 0 C m3/h	183,095	183,095	183,095	118,3804	118,3804	46,4752	71,9052	7,1905	64,7147
Cp kJ/kg-K	2,8105	3,6539	4,0803	3,8708	3,4358	14,2787	1,7545	1,5396	1,7769
Z factor	0,9993	1,0028	1,0032	1,0029	1,0002	1,0005	0,9927	0,9942	0,9924
Visc N-s/m2	1,08E-05	1,85E-05	2,29E-05	2,20E-05	1,87E-05	8,86E-06	9,45E-06	1,02E-05	9,37E-06
Th cond W/m-K	0,078	0,1433	0,1889	0,1436	0,1156	0,1718	0,0213	0,0206	0,0214
FLOW SUMMARIES
Stream No.	1	2	3	4	5	6	7	8	9
Stream Name
Temp K	298	567,2568	750	750	613,5513	298	298	298	298
Pres bar	1	10	10	10	1	1	1	1	1
Enth MJ/h	167,61	254,97	325,75	-84,979	-134,72	-0,0080855	-225,53	16,757	-242,29
Vapor mole fraction	1	1	1	1	1	1	1	1	1
Total kmol/h	8,1689	8,1689	8,1689	5,2816	5,2816	2,0735	3,2081	0,3208	2,8873
Flowrates in kmol/h
Ethane	0	0	0	2,8873	2,8873	0	2,8873	0	2,8873
Ethene	3,2081	3,2081	3,2081	0,3208	0,3208	0	0,3208	0,3208	0
Hydrogen	4,9608	4,9608	4,9608	2,0735	2,0735	2,0735	0	0	0
FLOW SUMMARIES
Stream No.	1	2	3	4	5	6	7	8	9	numery strumieni zgodne z schematem
Stream Name
Temp K	298	567,2568	750	750	613,5513	298	298	298	298
Pres bar	1	10	10	10	1	1	1	1	1
Enth MJ/h	167,61	254,97	325,75	-84,979	-134,72	-0,0080855	-225,53	16,757	-242,29
Vapor mass fraction	1	1	1	1	1	1	1	1	1
Total kg/h	100	100	100	100,0006	100,0006	4,1798	95,8208	9	86,8208
Flowrates in kg/h
Ethane	0	0	0	86,8208	86,8208	0	86,8208	0	86,8208
Ethene	90	90	90	9	9	0	9	9	0
Hydrogen	10	10	10	4,1798	4,1798	4,1798	0	0	0

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Sheet 2: UOPS1

CHEMCAD	6.1.4	Page	1
Job name:	przykład	Date:	2012-01-05	Time:	17:27:48
EQUIPMENT SUMMARIES
Compressor Summary
Equip. No.	1
Name
Pressure out bar	10
Type of Compressor	1
Efficiency	0,7
Actual power kW	24,2667	rzeczywista moc sprężarki
Cp/Cv	1,3208
Theoretical power kW	16,9867
Ideal Cp/Cv	1,3189
Calc Pout bar	10
Calc. mass flowrate	100
(kg/h)
Heat Exchanger Summary
Equip. No.	2
Name
1st Stream T Out K	750	obciążenie cieplne wymiennika ciepła służącego do ogrzewania strumienia - do wyliczenia kosztu zakupu w programie należy tę wartość przeliczyć na kW
Calc Ht Duty MJ/h	70,7783	0,0707783	GJ/h
LMTD Corr Factor	1
1st Stream Pout bar	10
Reactor Summary
Equip. No.	3
Name
Thermal mode	2
Temperature K	750	obciążenie cieplne reaktora
Heat duty MJ/h	-410,7301	-0,4107301	GJ/h
Key Component	2
Frac. Conversion	0,9
Reactor Pressure bar	10
Calc H of Reac.	-136133,0156
(kJ/kmol)
Stoichiometrics:
Ethane	1
Ethene	-1
Hydrogen	-1
Expander Summary
Equip. No.	4
Name
Pressure out bar	1
Type of Expander	1
Efficiency	0,75
Actual power kW	-13,8163	rzeczywista moc turbiny
Cp/Cv	1,1297
Theoretical power kW	-18,4218
Ideal Cp/Cv	1,128
Calc Pout bar	1
Component Separator Summary
Equip. No.	5	6	5	6
Name
Top Temp Spec	298	298
Bottom Temp Spec	298	298	obciążenia cieplne obu separatorów
Heat duty MJ/h	-90,8188	-0,0006	-0,0908188	-6E-07	GJ/h
Component No. 2		1
Component No. 3	1

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Sheet 3: THERM1

CHEMCAD	6.1.4	Page	1
Job name:	przykład	Date:	2012-01-05	Time:	17:27:48
COMPONENTS
	ID #	Name	Formula
1	3	Ethane	C2H6
2	22	Ethene	C2H4
3	1	Hydrogen	H2
THERMODYNAMICS
K-value model : SRK
IPP flag on
Enthalpy model : SRK
Liquid density :	Library
Std vapor rate reference temperature is 0 C.
Atmospheric pressure is	1,0132	bar.
SRK Parameters:
Bip A + B * T + C * T * T T Temperature in degree K
I	J	A	B	C
1	2	0,0123	0	0
1	3	-0,014	0	0
2	3	0,054	0	0

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Sheet 4: CONVERGE1

CHEMCAD	6.1.4	Page	1
Job name:	przykład	Date:	2012-01-05	Time:	17:27:48
Calculation mode : Sequential
Flash algorithm : Normal
Equipment Calculation Sequence
1	2	3	4	5	6
No recycle loops in the flowsheet.
Overall Mass Balance	kmol/h		kg/h
	Input	Output	Input	Output
Ethane	0	2,887	0	86,82
Ethene	3,208	0,321	90	9
Hydrogen	4,961	2,074	10	4,18
Total	8,169	5,282	100	100

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Sheet 5: TOPOLOGY1

CHEMCAD	6.1.4	Page	1
Job name:	przykład	Date:	2012-01-05	Time:	17:27:47
FLOWSHEET SUMMARY
Uop ID	Type	Label	Stream Numbers
1	COMP		1	-2
2	HTXR		2	-3
3	REAC		3	-4
4	EXPN		4	-5
5	CSEP		5	-6	-7
6	CSEP		7	-8	-9
Stream Connections
Stream	Equipment			Stream	Equipment			Stream	Equipment
	From	To			From	To			From	To
1		1		4	3	4		7	5	6
2	1	2		5	4	5		8	6
3	2	3		6	5			9	6