Again thak you for share this content. One question, Do you think that it's possible to simulate the Bio-OIL as non-conventional component since there is no available data about composition and only there is available overall yields? I suppose that will be necessary more data about properties of bio-oil yo simulate the condensation phase, but I am not sure if it is possible. Do you have any content similar like that?
Hm, but you would go into the fluidized bed with components that are partly only formed during the process and partly do not exist in the process. I think that would not be a plausible assumption. I would do a research in the literature. Perhaps there is now an approach for biomass conversion in fluidized beds.
@@kgengineeringsolutions l have reviewed research papers that have utilized Fluidized Bed Reactor for combustion of coal. In fact I am currently working on a project that utilizes fluidized bed reactor for combustion reaction and it is generating results.
In this model u gave the yield of the subproducts of pyrolysis before the start of the whole process. There`s anyway i can make a simulation of pyrolysis process to predict the yield of bio-oil, biochar and NCG? Ex: i want to know which biomass at my disposal, using a determinate tecnique (fast or slow), will be better to get the yield i need. Can i simulate this?
Hello sir, I am getting the following required data incomplete error ---- Calculator Block C-1 Block: DRIER Model: RYIELD Block: B2 Model: RYIELD VAPOR PRESSURE MODEL PL0XANT HAS MISSING PARAMETERS: PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT 4-ETH-02 PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT METHY-04 PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT (E)-2-01 PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT BENZA-01 ****PROPERTY PARAMETER ERROR ERRORS ENCOUNTERED IN CALCULATION OF VAPOR-LIQUID K-VALUES USING OPTION SET RKS-BM FOR KVL. ! Calculations stopped because of missing property parameters ---- how it can be eliminated
Again thak you for share this content.
One question, Do you think that it's possible to simulate the Bio-OIL as non-conventional component since there is no available data about composition and only there is available overall yields? I suppose that will be necessary more data about properties of bio-oil yo simulate the condensation phase, but I am not sure if it is possible. Do you have any content similar like that?
You're welcome. I once assumed a formula for bio oil. See the video th-cam.com/video/md4inypVGKs/w-d-xo.html. It might help you.
Can we use a fluidized bed reactor for combustion reactions after a yield reactor ? Just asking.
Hm, but you would go into the fluidized bed with components that are partly only formed during the process and partly do not exist in the process. I think that would not be a plausible assumption. I would do a research in the literature. Perhaps there is now an approach for biomass conversion in fluidized beds.
@@kgengineeringsolutions l have reviewed research papers that have utilized Fluidized Bed Reactor for combustion of coal. In fact I am currently working on a project that utilizes fluidized bed reactor for combustion reaction and it is generating results.
How do i calculate the energy generated from each part biochar, bio-oil and gases?
Do you mean the energy content of the three products?
In this model u gave the yield of the subproducts of pyrolysis before the start of the whole process. There`s anyway i can make a simulation of pyrolysis process to predict the yield of bio-oil, biochar and NCG? Ex: i want to know which biomass at my disposal, using a determinate tecnique (fast or slow), will be better to get the yield i need. Can i simulate this?
As far as I know there is no method.
Hello sir, I am getting the following required data incomplete error ---- Calculator Block C-1
Block: DRIER Model: RYIELD
Block: B2 Model: RYIELD
VAPOR PRESSURE MODEL PL0XANT HAS MISSING PARAMETERS:
PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT 4-ETH-02
PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT METHY-04
PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT (E)-2-01
PLXANT/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT BENZA-01
****PROPERTY PARAMETER ERROR
ERRORS ENCOUNTERED IN CALCULATION OF VAPOR-LIQUID K-VALUES USING
OPTION SET RKS-BM FOR KVL.
! Calculations stopped because of missing property parameters ---- how it can be eliminated
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