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1. 发明专利

PL161842B1 METHOD OF OBTAINING HYDROGEN FROM THE COKING GAS 未知
公开(公告)号：PL161842B1
公开(公告)日：1993-08-31
申请号：PL27849489
申请日：1989-03-23
申请人： INST CIEZKIEJ SYNTEZY ORGA , ZAKLADY KOKSOWNICZE , ZAKLADY AZOTOWE KEDZIERZYN , ZAKLADY CHEM BLACHOWINA
发明人： BUDNER ZBIGNIEW , MORAWIEC BERNARD , WASILEWSKI JERZY , KLIMIEC JACEK , MORAWSKI ROMUALD , JAMORSKI KAZIMIERZ , WANECKI FRANCISZEK , BROCHOCKI WITOLD , DRAGUN HENRYK , CHMIELEWSKI KONSTANTY , RETERSKA ZDZISLAWA , JERZYK WITOSLAW , SIEJA EUSTACHY , NAWROT HENRYK , CYPRYCH WLODZIMIERZ , GRABIEC LUCJAN , PILARCZYK HENRYK , NIEDZIELA JAN , GORECKI JANUSZ
IPC分类号： B01D53/02 , C01B3/56 , C10K1/32
摘要： 1. A method of obtaining of hydrogen from coke-oven gas consisting in selective adsorption of constituents of gases on solid sorbents and then their desorption by means of PSA, directing gases to for the process of conversion and then repetition of adsorption and separation of the obtained gases with the use of PSA, characterised in that the gas is separated in the first adsorption installation by means of PSA, producing a stream of hydrogen gas, of content maximum 90 moles percent of hydrogen and at least 8-10 moles percent of carbon monoxide and a stream of methane gas consisting of maximum 4.0 moles percent of carbon monoxide and at least 70 moles percent of methane, which stream is compressed and purified with known methods and the stream of hydrogen gas is compressed until reaching the pressure of 3.0-4.0 MPa and is subject to the process of conversion with water vapour, next the converted hydrogen gas, consisting of 0.1-3 moles percent of carbon monoxide is separated in the second adsorption installation PSA, however, the residue gas contains maximum 20 capacity percent of hydrogen.

3. 发明专利

PL256908A1 METHOD OF OBTAINING POLYPROPYLENE OLIGOMERS IN REACTORS OF ADIABATIC PLATE TYPE 未知
公开(公告)号：PL256908A1
公开(公告)日：1987-10-05
申请号：PL25690885
申请日：1985-12-17
申请人： INST CIEZKIEJ SYNTEZY ORGA , ZAKLADY CHEM BLACHOWINA
发明人： BUDNER ZBIGNIEW , MORAWIEC BERNARD , KLIMIEC JACEK , TKACZ BOGUSLAW , BEK TEODOR , PILARCZYK HENRYK , MARSZYCKI JERZY , BUCZEK LEONARD , CZYZ JERZY , KOLT JOZEF
IPC分类号： C07C20060101 , C07C2/18 , C07C11/02 , C07C

4. 发明专利

PL251856A1 METHOD OF SEPARATING ETHYLENE AND PROPYLENE FROM GASES,IN PARTICULAR COKE OVEN ONES 未知
公开(公告)号：PL251856A1
公开(公告)日：1986-08-12
申请号：PL25185685
申请日：1985-02-04
申请人： INST CIEZKIEJ SYNTEZY ORGA , ZAKLADY KOKSOWNICZE IM POWSTAN
发明人： BUDNER ZBIGNIEW , MORAWIEC BERNARD , SITKIEWICZ JADWIGA , MORAWSKI ROMUALD , WANECKI FRANCISZEK , BORSZ PIOTR
IPC分类号： C07C20060101 , C07C7/11 , C07C11/04 , C07C11/06 , C07C

6. 发明专利

PL162570B1 METHOD OF REFINING MACRO-AND MICROCRYSTALLINE PARAFFINS 未知
公开(公告)号：PL162570B1
公开(公告)日：1993-12-31
申请号：PL28494190
申请日：1990-04-24
申请人： INST CIEZKIEJ SYNTEZY ORGA
发明人： BUDNER ZBIGNIEW , KLIMIEC JACEK , MORAWIEC BERNARD , TKACZ BOGUSLAW
IPC分类号： C07C7/163 , C10G67/06

7. 发明专利

PL255063A1 METHOD OF CATALYTICALLY REFINING CRUDE PHTALIC ANHYDRIDE 未知
公开(公告)号：PL255063A1
公开(公告)日：1987-03-23
申请号：PL25506385
申请日：1985-08-19
申请人： INST CIEZKIEJ SYNTEZY ORGA
发明人： BUDNER ZBIGNIEW , KORCZYNSKI MARIAN , TURZA IZABELLA , ZEGAROWSKA EMILIA , MORAWIEC BERNARD , SITKIEWICZ JADWIGA
IPC分类号： C07D20060101 , C07D307/83 , C07D

8. 发明专利

PL285902A1 METHOD OF OBTAINING PROPIONIC ACID 未知
公开(公告)号：PL285902A1
公开(公告)日：1992-01-13
申请号：PL28590290
申请日：1990-07-02
申请人： INST CIEZKIEJ SYNTEZY ORGA
发明人： KLIMIEC JACEK , BUDNER ZBIGNIEW , TKACZ BOGUSLAW , MORAWIEC BERNARD , KOLODENNY RYSZARD , MALAJKA JOZEF
IPC分类号： C07C53/122

9. 发明专利

PL284941A1 METHOD OF REFINING MACRO-AND MICROCRYSTALLINE PARAFFINS 未知
公开(公告)号：PL284941A1
公开(公告)日：1991-11-04
申请号：PL28494190
申请日：1990-04-24
申请人： INST CIEZKIEJ SYNTEZY ORGA
发明人： BUDNER ZBIGNIEW , KLIMIEC JACEK , MORAWIEC BERNARD , TKACZ BOGUSLAW
IPC分类号： C07C7/163 , C10G67/06

10. 发明专利

PL162440B1 METHOD OF HYDROGEN SEPARATION FROM GAS MIXTURES 未知
公开(公告)号：PL162440B1
公开(公告)日：1993-12-31
申请号：PL28314989
申请日：1989-12-29
申请人： INST CIEZKIEJ SYNTEZY ORGA
发明人： BUDNER ZBIGNIEW , MORAWIEC BERNARD , STADNICKI KRZYSZTOF , KLIMIEC JACEK , KOLODENNY RYSZARD , CHMIELEWSKI KONSTANTY , NAWROT HENRYK , RETERSKA ZDZISLAWA , SIEJA EUSTACHY , PIETRONSKI JOZEF , JERZYK WITOSLAW
IPC分类号： B01D53/02 , C01B3/56
摘要： Method of educing hydrogen from gas mixtures by means of adsorption method PSA in an adsorption installation containing adsorbers filled with solid sorbent or layers of sorbents, operating according to a cyclically repeated schedule including technological operations of adsorption, pressure lowering, sorbent washing and pressure increasing, which are performed by opening cut-off valves according to a specified program, due to which proper gas streams flow in or out of proper adsorbers characterised in that, after the adsorption, the two-stage pressure lowering, cocurrent with respect to the gas flow in the adsorption stage is performed in the adsorber, and the gas from the first stage of cocurrent pressure lowering is used for the first stage counter current pressure increasing in another adsorber, and the gas obtained from the second stage of cocurrent pressure lowering is used for second stage cocurrent pressure increasing in another adsorber, and next, the operation of counter current pressure lowering and counter current sorbent washing in the adsorber with the use of hydrogen obtained during the adsorption stage are successively performed, and received gas streams from such two operations are joined with each other and removed from the installation as the tail gas, and after such operations, the two-stage pressure increasing in the adsorber is performed, successively, the cocurrent one in the second stage and counter current one in the first stage, and final pressure increasing and compensation with respect to the pressure in the adsorption stage is performed by counter current supply to the adsorber of the part of hydrogen obtained during the adsorption stage, and the operations of cocurrent pressure lowering in the adsorber of the first and second stage are coordinated in time with proper operations of the second stage cocurrent pressure increasing and the first stage counter current pressure increasing, both performed in other adsorbers, the operations of counter current sorbent washing with hydrogen and counter current pressure compensation with hydrogen are performed in the installation in an alternate manner during the whole cycle, and adsorption operations performed in consecutive adsorbers are shifted in time by two strokes with respect to each other and the duration of one stroke is 30-90 seconds.

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