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1. 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

3. 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

4. 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

5. 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

6. 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

7. 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.

9. 发明专利

PL284248A1 METHOD OF OBTAINING BUTYL ALCOHOLS 未知
公开(公告)号：PL284248A1
公开(公告)日：1991-09-09
申请号：PL28424890
申请日：1990-03-08
申请人： INST CIEZKIEJ SYNTEZY ORGA
发明人： KLIMIEC JACEK , BUDNER ZBIGNIEW , TKACZ BOGUSLAW , KOLODENNY RYSZARD , CHOWANIEC JERZY , MIGOCZ JOACHIM , MALAJKA JOZEF , GOLEBOWSKI RYSZARD , WARCHOL MIECZYSLAW , GARBACIAK JERZY , MORAWIEC BERNARD
IPC分类号： C07C29/141 , C07C31/12

10. 发明专利

PL270958A1 METHOD OF OBTAINING PROPYLENE OLIGOMERS 未知
公开(公告)号：PL270958A1
公开(公告)日：1989-09-04
申请号：PL27095888
申请日：1988-03-01
申请人： INST CIEZKIEJ SYNTEZY ORGA
发明人： TKACZ BOGUSLAW , BUDNER ZBIGNIEW , KLIMIEC JACEK , MORAWIEC BERNARD , KOLODENNY RYSZARD , WIETRZYNSKA-LALAK ZOFIA
IPC分类号： C07C2/18 , C08F20060101 , C08F

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