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Patent US4661570 - Method of continuous polymerization - Google PatentsSearch Images Maps Play YouTube News Gmail Drive More »Sign inAdvanced Patent SearchPatentsA solid polymerization product is continuously produced from a liquid stock by employing a continuous agitator-mixer type reactor including two parallel shafts rotatable in same direction or in opposite directions, a multiplicity of paddles mounted on each of the shafts, and a barrel with its inner periphery...http://www.google.com/patents/US4661570?utm_source=gb-gplus-sharePatent US4661570 - Method of continuous polymerizationAdvanced Patent SearchPublication numberUS4661570 APublication typeGrantApplication numberUS 06/853,096Publication dateApr 28, 1987Filing dateApr 17, 1986Priority dateApr 17, 1985Fee statusPaidAlso published asCA1265287A1, DE3673682D1, EP0198719A2, EP0198719A3, EP0198719B1Publication number06853096, 853096, US 4661570 A, US 4661570A, US-A-4661570, US4661570 A, US4661570AInventorsMasami Yamawaki, Shuichi Chino, Tsuyoshi Minamisawa, Masaaki NakamuraOriginal AssigneePolyplastics Co., Ltd.Export CitationBiBTeX, EndNote, RefManPatent Citations (2), Referenced by (1), Classifications (10), Legal Events (6) External Links: USPTO, USPTO Assignment, EspacenetMethod of continuous polymerization
US 4661570 AAbstract
A solid polymerization product is continuously produced from a liquid stock by employing a continuous agitator-mixer type reactor including two parallel shafts rotatable in same direction or in opposite directions, a multiplicity of paddles mounted on each of the shafts, and a barrel with its inner periphery proximate to the outer peripheries of the paddles, said paddles being arranged so that the major axis end of each paddle on one of the shafts is allowed to periodically come close to the minor axis ends of a corresponding paddle on the other shaft, said reactor being such that feed stock is charged from an inlet port provided at one end of the longitudinal of the reactor and polymerization product is discharged from an outlet port provided at the other end, said method of continuous polymerization being characterized in that the rear-side portion of the reactor including the outlet port is raised so that the major axis of the reactor has a slope angle of 1�-10� relative to the horizontal, whereby reaction is allowed to take place in the reactor as installed in such inclined state.
1. A method of continuous polymerization for continuously producing a solid polymerization product from a liquid stock by employing a continuous agitator-mixer type reactor including two parallel shafts rotatable in same direction or in opposite directions, a multiplicity of paddles mounted on each of the shafts, and a barrel with its inner periphery proximate to the outer peripheries of the paddles, said paddles being arranged so that the major axis end of each paddle on one of the shafts is allowed to periodically come close to the minor axis end of a corresponding paddle on the other shaft, said reactor being such that feed stock is charged from an inlet port provided at one end of the longitudinal of the reactor and polymerization product is discharged from an outlet port provided at the other end, said method of continuous polymerization being characterized in that the rear-side portion of the reactor including the outlet port is raised so that the major axis of the reactor has a slope angle of 1-10 degrees relative to the horizontal, whereby reaction is allowed to take place in the reactor as installed in such inclined state.
2. The method of continuous polymerization as set forth in claim 1 wherein the liquid stock is trioxane or a mixed liquid composed of trioxane as a principal ingredient and a copolymer which is copolymerizable therewith, and wherein the solid polymerization product is a trioxane polymer or trioxane copolymer.
3. The method of continuous polymerization as set forth in claim 1, wherein said slope angle is from about 1 to about 5 degrees relative to the horizontal.
4. The method of continuous polymerization as set forth in claim 3 wherein said slope angle is about 1 degree relative to the horizontal.
5. The method of continuous polymerization according to claim 3 wherein said slope angle is about 3 degrees relative to the horizontal.
6. The method of continuous polymerization as set forth in claim 3 wherein said slope angle is about 5 degrees relative to the horizontal.
7. The method of continuous polymerization as set forth in claim 1, wherein the degree of conversion of said liquid stock into polymer is at least about 70%.
8. The method of continuous polymerization as set forth in claim 1, wherein said liquid stock includes at least one ingredient selected from the group consisting of ethylene oxide and vinyl chloride.
9. The method of continuous polymerization as set forth in claim 1, wherein said liquid stock includes at least one of dibutyl etherate, boron trifluoride, phosphorous pentafluoride, tin tetrachloride, perchloric acids or salts thereof.
10. The method of continuous polymerization is set forth in claim 1, wherein said liquid stock includes methylal.
The present invention relates to a method of polymerization for continuously producing a polymerization product in fine particle form from a substantially liquid-form stock.
More specifically, the invention relates to a method of continuous polymerization for producing a solid polymerization product in fine particle form from a liquid stock in a so-called continuous agitatormixer type polymerization reactor including two parallel shafts rotatable in same direction or in opposite directions, a multiplicity of paddles mounted on each of the shafts, and a barrel with its inner periphery proximate to the outer peripheries of the paddles, characterized in that the rear-side portion of the reactor including an outlet port is raised so that the major axis of the reactor has a slope angle of 1�-10� relative to the horizontal, whereby reaction is allowed to take place in the reactor as installed in such inclined state.
Generally, where polymerizable liquid monomers are polymerized in the presence of a suitable polymerizing catalyst, there are two different cases, namely, one wherein the polymeric mass produced is soluble in the monomers and therefore the mass forms a viscous liquid mass, which in turn is caused to form a highly viscous material as polymerization progresses, and the other wherein the polymeric mass is insoluble in the monomers and accordingly, as polymerization progresses, there occurs a change of phase such that the mass undergoes a change from liquid state into slurry state before it is finally separated out in the form of a completely solid polymerization product. The invention relates to a system of the latter case. A typical example of continuous manufacture of a solid polymerization product through such polymerization reaction as involved in the latter case is polyvinyl chloride production through bulk polymerization, and another is polyacetal resin production through bulk polymerization In the following description, therefore, a method of manufacturing polyacetal resin is mainly taken up.
It is already known to produce a polyacetal resin by using such cation active polymerizing catalysts as boron trifluoride, phosphorus pentafluoride, tin tetrachloride, perchloric acid, or salts thereof or complex salt and through monopolymerization of trioxane or through copolymerization with cyclic ethers such as trioxane and ethylene oxide, or with cyclic formal or the like. Such method is in actual practice on an industrial scale. In the process of such polymerization or copolymerization, as already stated, so-called phase change takes place as polymerization progresses, so that the polymeric mass changes into a solid polymeric mass via a short period of its slurry state. Further, in a so-called bulk polymerization method wherein virtually no diluent is present, reaction is so fast that the phase change is very abrupt; hence, it is no easy task to control the reaction. For example, if such polymerization or copolymerization reaction is carried out in static condition, a large bulky and tough product is produced in an instantaneously short time, so that material handling in the subsequent crushing, cleaning, and refining stages is extremely difficult. Moreover, because of internally accumulated polymerization heat, temperature control is almost impossible, with the result of quality deterioration and unfavorable rate of conversion. Therefore, in view of such specific aspect of reaction and in order to prevent formation of such bulky polymerization product and to allow efficient production of a fine-particle polymerization product which is comparatively quality-stable, a number of approaches have been proposed. One basic concept common to those approaches is utilization of an extruder type polymerization reactor having a two-parallel-shaft agitator arrangement.
The concept of utilizing such extruder type reactor having a two-parallel-shaft agitator construction for the purpose of manufacturing polyacetal resins, pioneered by a proposal to use a two-shaft screw type extruder as disclosed in Japanese Published Examined patent Application Nos. 47-629 and 47-42145, and a proposal to employ a two-shaft mixer consisting of a combination of screws and elipsoidal disc paddles, with subsequent development and improvements, led to a number of proposals including Japanese Published Unexamined patent application Nos. 53-86794, 56-38313, and 58-32619 - 21. There are two types, one such that the parallel two shafts rotate in same direction and the other such that the shafts rotate in opposite (different) directions, both having similar functions. The former type is claimed as having good self-cleaning characteristics; and in the area of the latter type, there has been proposed an arrangement such that shear force is variably effected automatically in a desired direction according to the phase change, as disclosed in Japanese Published Unexamined patent application. At present, manufacturing techniques employed for industrial production of polyacetal resin are largely based on said proposal.
Recently, the demand for polyacetal resins has been constantly on the increase, and in view of the fact that high quality is demanded of the resin in thermal stability characteristics in particular, the state of the art for production process is not always satisfactory. Further efforts are desired for improvement of polymerization product yield or conversion rate per unit of equipment, and also for improvement in quality of polymerization products through more effective stabilization treatment. When a two-parallel-shaft rotary agitator type reactor incorporating various features based on aforesaid inventive proposals, with modified paddle configuration and arrangement, is employed in producing polyacetal resins, it is indeed possible to obtain a polymerization product of a relatively fine particle form at a high conversion rate, if the equipment is of a small type of laboratory scale. However, as the size of the installation becomes larger, results obtained are not necessary satisfactory. For example, a polymerization product of coarse-particle size, e.g., small-finger size, rather than fine-particle size, is produced in a larger proportion. Further, a thicker scale of polymeric matter is likely to deposit on the inner wall of the equipment, thus causing a decrease in heat transfer efficiency, which inevitably results in decreased conversion rate and lower product quality. In such case, the polymerization product from the reactor is often ground and refined by a grinder, and then led to a so-called quenching stage in which it is subjected to stabilization treatment, such as cleaning, under good cooling condition, before the product enters the subsequent stage. Where operation is carried out continuously, masses of polymeric product being continuously turned out involve considerable fluctuations in quality and furthermore the flow in the process of polymeric masses converted from the stock is subject to considerable pulsation; therefore, attempts to control reaction are not always effective to the satisfaction of the accuracy requirements.
The functions required of a two-shaft agitator type reactor of the kind include:
(a) fast and homogeneous blending of catalists and polymerizable monomers, i.e., trioxane or cyclic compound monomers copolymerizable with trioxane;
(b) prevention of polymeric particle adhesion at an initial stage where a polymeric product is separated out as polymerization initiates, that is, at a stage where the polymeric product is in slurry condition (high shear force);
(c) prevention of solid polymeric product from bulking, or grinding of bulk polymeric product (high shear force);
(d) retention of within-reactor self-cleaning characteristics (prevention or removal of deposit retention);
(e) retention of good efficiency of heat transfer to fine-particle polymerization product (retention of the specified polymerization temperature, relaxation or reduction of reaction temperature internal build-up); and
(f) prevention of product flow from pulsation throughout the process of from stock introduction and to product discharge.
Even if various improvements are made in paddle configuration and/or paddle arrangement, it is practically impossible that all these requirements are fully satisfied within one reactor. The reason for aforesaid difficulty of sealing up reactors of the type lies in this point. More especially, it must be noted that phase change from the liquid to the solid is abrupt because the speed of polymerization reaction is very fast, from which fact it follows that the density change involved is considerable and that the reactor contents also undergo considerable volumetric change. As a result of such phenomena, the fill level of reactor contents varies locally in the axial direction; therefore, pulsation is caused to the flow of product, which leads to fluctuations in agitation or grinding efficiency, and ultimately to a lower conversion rate and lower product quality. In order to overcome these problems, measures are often taken to regulate the flow by adopting a suitable combination of "feed" type and "reverse (back feed)" type paddles in paddle arrangement. However, such approach may often involve troubles, such as excessive power consumption, overloading, and reactor content blocking, during operation, and is not always useful for adequate regulation purposes. In Japanese Published Unexamined patent application No. 53-86794, it is proposed to divide the polymerization process into two stages, that is, a first stage in which a self-cleaning type reactor is employed, and a second stage in which a pin-mixer type heat-exchange reactor is employed. However, the proposal gives no basic measure for overcoming the difficulties involved in the first-stage reactor.
From the aforesaid view points, the present inventors directed their research efforts toward improving the operating characteristics of a parallel two-shaft agitator-mixer type polymerization reactor and achieving efficient production of polymerization products in fine particle form, and as a result they arrived at the present invention. Accordingly, the invention provides a method of continuous polymerization for producing a solid polymerization product from a liquid stock by employing a so-called continuous agitator-mixer type reactor including two parallel shafts rotatable in same direction or in opposite directions, a multiplicity of paddles mounted on each of the shafts, and a barrel with its inner periphery proximate to the outer peripheries of the paddles, said paddles being arranged so that the major axis end of each paddle on one of the shafts is allowed to periodically come close to the minor axis end of a corresponding paddle on the other shaft, said reactor being such that feed stock is charged from an inlet port provided at one end of the longitudinal of the reactor and polymerization product is discharged from an outlet port provided at the other end, said method of continuous polymerization being characterized in that the rear-side portion of the reactor including the outlet port is raised so that the major axis of the reactor has a slope angle of 1�-10� relative to the horizontal, whereby reaction is allowed to take place in the reactor as installed in such inclined state. Hitherto, it has been an established concept that a two-shaft rotary agitator-mixer type reactor should be operated in a level condition, but the present invention, unprejudiced by such fixed idea, was made under an entirely new and novel concept which led to the finding of the features characterizing the invention.
That is, the method of the invention is characterized in that the reactor is installed with its axis inclined at a certain angle or more to the horizon. This arrangement permits satisfactory polymerization control during continuous operation of the reactor: discharge variations can be minimized; polymerization reaction can be stabilized, with reduced internal temperature fluctuations; conversion rates for polymerization products can be improved, with reduced conversion fluctuations.
If the slope angle of the reactor is less than 1�, no sufficient advantage of the invention may be obtained. If the slope angle is more than 10�, the mechanism which supports the rotatable shafts and provides rotation power is subject to considerable load, so that troubles may be encountered during any prolonged operation; further, difficulties may arise in conjunction with hermetic maintenance of gland seals. Therefore, such high slope angle is not practical. In order to obtain good operating efficiency and to take good advantage of the invention, a preferred range of slope angles is 1�-5�.
For paddles mounted on the rotatable shafts in the reactor according to the invention, any known type of paddle may be used without particular limitation. By way of example, several sectional paddle configurations (sections perpendicular to the agitator shafts) are shown in FIG. 3. Various types of paddles, such as so-called convex lens-type, elipsoid-type, and quasi-triangle, or those types provided at front end with some notch or saw-tooth feature for scraper effect, may be employed according to the circumstance or condition involved. It is also possible to use eccentric disc type or eccentrically transformed disc type paddles. In effect, these types of paddles may be suitably selected and suitably arranged in combination according to the polymerization condition or aspect involved. Rather, one feature of the invention lies in the fact that such suitable combinations can be broadly selected.
For the two parallel shaft agitator type reactor employed in the method of the invention, it is desired that it can be industrially manufactured at low cost, and that the clearance between the front end of each paddle and the inner periphery of the barrel is less than 2%, preferably less than 1%, of the circumcircle diameter of the paddle and is free of variation or deviation due to major axis deformation. If consideration is taken of both machining accuracy and operational safety, L/D (where L is the length of the reactor, and D is the inner diameter thereof) should normally be less than 20, or preferably less than 15. On the other hand, if sufficient conversion is to be attained, L/D should preferably be more than 5. In order to obtain the desired fine-particle polymerization product, it is desired that the rotational speed of the agitator shafts should be within the range of 0.1-1.0 m/sec in terms of peripheral speed at the front edge of the paddle. In the method of the invention, however, the desired product can be effectively obtained even if the speed is less than 0.1 m/sec. Referring to the direction of rotation of the two shafts, two cases may be considered, i.e., rotation in same direction and rotation in opposite directions, as earlier mentioned; and the method of the invention may be equally applied in either case.
As already stated, the invention relates to a polymerization method for producing a solid polymerization product from a liquid stock, or in other words, a polymerization method of such system that the polymeric masses are insoluble in the material monomers and that a completely solid polymerization product is separated out as polymerization progresses. As far as such system is concerned, the method of the invention can be widely applied. More preferably, the method is employed for the purpose of polymerizing vinyl chloride, or homopolymerizing or copolymerizing trioxane. In the case of trioxane copolymerizing, there is no particular limitation as to copolymerizable monomers in a system wherein trioxane is contained as a principal ingredient in an amount of more than 50 mol%. Nor is there any limitation on the polymerizing catalyst to be used. Needless to say, a small amount of anhydrous inert solvent or molecular-weight regulator, or other additive may be effectively used.
Advantages of the invention are apparent from what has been described above. To sum up, unlike the conventional method which employs a two-shaft rotary agitator type reactor installed in level position, the method of the invention employs such reactor installed with a suitable slope angle to the horizon. Superficially, the mechanical arrangement employed in the invention may be similar to the one conventionally employed; however, the arrangement is advantageous in that it permits the fill rate of reactor contents to be readily kept constant in the direction of the major axis, in that the fill level can be readily adjusted, and in that any abrupt phase change or volumetric change can be readily relaxed, there being no possibility of substantial fluctuation in agitation efficiency. Indeed, the invention is based on a novel and unique concept as evidenced by these amazingly good improvements in reactor functions. According to the continuous polymerization method of the invention, continuous polymerization reaction can be steadily carried out even where a large-scale reactor is employed, and thus polymerization products of good and uniform quality can be obtained in the form of particle mass of a desired configuration and size and at a high yield.
Examples of the method of the invention will now be described with rerence to the drawings wherein like numerals designate similar parts.
FIG. 1 is a longitudinal section of a reactor of the class useful in practicing the inventive method;
FIG. 2 illustrates paddle arrangements which may be used in connection with the reactor of FIG. 1;
FIG. 3 details alternate paddle designs; and
FIG. 4 shows for various slope angles of a reactor the relationship between fill level and axial position.
By employing a two-shaft agitator type continuous polymerization reactor as shown in FIG. 1, with paddles having such sectional configuration as shown in FIG. 3(1) and arranged in such pattern as shown in FIG. 2, and under such common reaction conditions as described hereinafter, experiments were conducted for a number of cases with slope angle θ varied from case to case, namely, 0� (Comparative Example), 1�, 2�, 3�, and 5� (Examples 1, 2, 3, and 4). Needles to say, the interior of the reactor was thoroughly cleaned prior to the start of operation for each example.
In FIG. 1, numeral 1 is a stock inlet port, 2 is a product outlet port, 3 is a barrel body, 4 is a polymerizing catalyst inlet port, and 5 and 5' are bearings for the two shafts. Numeral 6 is a jacket surrounding the outer periphery of the barrel and divided into three sections. Shown by 7 are thermocouples mounted at temperature measuring junctions 1-6. (There is no limitation as to the number and locations of thermocouples, of course.) It is noted that θ denotes an angle which the axis makes with the horizon.
FIG. 2 is a schematic illustration of types of paddles and one example of their arrangement corresponding to FIG. 1; in the figure, each rectangle expresses a pair of paddles having a convex lenslike section without twist, and each rectangle with an oblique line denotes a pair of forward feed paddles (shown by □) or a pair of backward feed paddles (shown by □), as the case may be. Numerals at the bottom denote numbers of paddles counted from the inlet port.
A stock consisting of trioxane monomers mixed with 2.5% of ethylene oxide and 500 ppm of methylal as a regulator was introduced through the inlet port at a per-hour rate of 10 parts by weight, and a polymerizing catalyst consisting of a cyclohexane solution of boron trifluoride and dibutyl etherate was introduced through the catalyst inlet port 4 at a rate equivalent to 34 ppm relative to the polymerizable monomers. Oil heated to 90� C. was circulated through the jacket 6 for heating the reactor, and the rotational speed of the two shafts was maintained at 50 rpm.
Polymerization products as discharged from the outlet port 2 were sampled from time to time for measurement of their detention time, discharge rate, degree of conversion, and polymerization product melt index (MI). Variations in the measurements were examined. Also, internal temperature changes were recorded.
Meanwhile, in the individual examples and comparative example, reaction was suspended after some 3-4 hours of operation and fill levels of contents in the reactor were examined. Results of these measurements are shown together in Table 1 and FIG. 4.
TABLE 1__________________________________________________________________________        Comp. Example                    Example                          Example                                Example        example              1     2     3     4__________________________________________________________________________Slope angle θ�        0     1.    2     3     5Detention time (min)        6.5˜8.3              8.0   8.1   7.7   8.3MI of polymerization        5.2˜8.3              4.6˜5.1                    4.5˜4.6                          4.2˜5.1                                4.6˜5.2productDegree of conversion (%)        62.2˜66.8              74.4˜77.3                    78.0˜78.1                          76.2˜78.4                                78.2˜79.3Variations in conversion        4˜6              1.9   1.7   1.3   1.3(δ/-x � 100) (%)Temperature variations        1.4˜1.7              1.2˜1.6                    1.2   0.5˜0.7                                0.5˜0.6(at measuring junction 2in FIG. 1) (�C.)Variations in discharge        >20    8˜11                    7˜8                          8˜9                                10rate (δ/-x � 100) (%)__________________________________________________________________________ -x: mean value δ: standard deviation
As is apparent from Table 1, it has been confirmed that by operating the reactor as installed with a certain slope angle or more it is possible to reduce discharge variations significantly, statilize polymerization reactor, minimize internal temperature fluctuations, attain improved conversion into polymerization product, with reduced variation therein, and further to stabilize the M1 of polymerization product at a low level. Again, as can be seen from FIG. 4, it has been found that by placing the reactor at an angle of inclination to the horizon the fill rates of contents in the reactor can be equalized, which fact may be taken as an evidence supporting the Table 1 data.
Little deposit, if any, was found present on the inner wall of the reactor; and the polymerization product was of a fine particle size of the order of less than 2 mm dia., with a minor proportion of particles of not more than 3 mm dia.
Patent CitationsCited PatentFiling datePublication dateApplicantTitleUS3538067 *Feb 8, 1967Nov 3, 1970Saint GobainMethod for the polymerization of vinyl chloride in massUS4383093 *Jun 3, 1981May 10, 1983Mitsui Petrochemical Industries Ltd.Tubular polymerization reactor, and process for polymerization* Cited by examinerReferenced byCiting PatentFiling datePublication dateApplicantTitleUS5254647 *May 24, 1991Oct 19, 1993Idemitsu Petrochemichal Co., Ltd.Process for producing styrene-based polymers* Cited by examinerClassifications U.S. Classification526/88International ClassificationC08G2/10, C08F2/00, C08G2/00, B01J19/20Cooperative ClassificationC08G2/00, B01J2219/182, B01J19/20European ClassificationB01J19/20, C08G2/00Legal EventsDateCodeEventDescriptionApr 17, 1986ASAssignmentOwner name: POLYPLASTICS CO., LTD., 30, AZUCHIMACHI 2-CHOME, HFree format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:YAMAWAKI, MASAMI;CHINO, SHUICHI;MINAMISAWA, TSUYOSHI;AND OTHERS;REEL/FRAME:004540/0641Effective date: 19860328Jul 16, 1990FPAYFee paymentYear of fee payment: 4Sep 28, 1994FPAYFee paymentYear of fee payment: 8Dec 6, 1994REMIMaintenance fee reminder mailedJul 11, 1995FPExpired due to failure to pay maintenance feeEffective date: 19950503Sep 28, 1998FPAYFee paymentYear of fee payment: 12RotateOriginal ImageGoogle Home - Sitemap - USPTO Bulk Downloads - Privacy Policy - Terms of Service - About Google Patents - Send FeedbackData provided by IFI CLAIMS Patent Services

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M B Daniélov - Semantic Scholar
M B Daniélov
A V Utin8
O V Shcherbinina1
N I Khodzhaev1
8A V Utin
1O V Shcherbinina
1A. N. Kucher
1N I Khodzhaev
1Zh. O. Soltobaeva
[Inbreeding in the Samarkand region].
Data on the frequency of inbreeding in some isolated populations of Samarkand region are given. Statistically significant differences were established in the frequency of inbreeding in separate… (More)
[Preliminary assessment of genetic load (in lethal equivalents) according to findings from consanguineous marriages].
[Medico-genetic consultation of families of oligophrenic patients (according to empirical risk findings)].
M B Daniélov, A. V. Utin
On the basis of the careful etiological and clinical differentiation of different types of oligophrenia observed in 402 probands of mentally retarded patients, the authors have developed a table of… (More)
[Genetic analysis of microcephaly].
A clinical genetic examination of 22 cases of hereditary microcephaly in 11 families was carried out. Parent consanguinity (first and second cousins) was ascertained in 7 families. Genetic analysis… (More)
[A study of heredity in epilepsy under inbred conditions].
A. V. Utin, M B Daniélov
[Undifferentiated X-linked oligophrenias].
In the course of investigation of 262 families with non-differentiated forms of oligophrenias it is established that in 48 families (18.3%) mental deficiency in sibs is caused by pathological… (More)
[The genetic relationship between convulsions in childhood and epilepsy (a clinico-genealogic study under inbreeding conditions)].
[Genetic factors in the etiology of undifferentiated oligophrenia].
A clinico-genetical study of 262 families of patients with clinically nondifferentiated oligophrenia established that genetical factors play an important role in its etiology. According to the… (More)
[Medico-genetic consultation and clinico-social prognosis of epileptics].
A. V. Utin, M B Daniélov, Olga V Shcherbinina
The results of the clinical-genetic examinations of 291 families of the general population are discussed. The authors present tables of empirical risk of recurrent epilepsy and lesser epileptic… (More)
[Problem of the etiology of undifferentiated oligophrenia].
On the basis of examination of 150 families with clinically and etiologically undifferentiated oligophrenias the authors have studied a possible contribution of genetic and psychosocial factors to… (More)

value: This website is an artificial-intelligence backed search engine for academic publications developed at the Allen Institute for AI and publicly released in November 2015. It uses advances in natural language processing to provide summaries for scholarly papers.


text:
Sellebjerg F[au] - PubMed - NCBI
Search: Sellebjerg F[au]
Select item 31428180 1.
The transcriptome of peripheral blood mononuclear cells in patients with clinical subtypes of late age-related macular degeneration.
Subhi Y, Nielsen MK, Molbech CR, Liisborg C, Søndergaard HB, Sellebjerg F, Sørensen TL.
Immun Ageing. 2019 Aug 15;16:20. doi: 10.1186/s12979-019-0160-0. eCollection 2019.
31428180
Select item 31276927 2.
Select item 31242590 3.
Relationship between Multiple Sclerosis-Associated IL2RA Risk Allele Variants and Circulating T Cell Phenotypes in Healthy Genotype-Selected Controls.
Buhelt S, Søndergaard HB, Oturai A, Ullum H, von Essen MR, Sellebjerg F.
Cells. 2019 Jun 25;8(6). pii: E634. doi: 10.3390/cells8060634.
31242590
Select item 31206160 4.
Select item 31129415 5.
Illegal cannabis use is common among Danes with multiple sclerosis.
Gustavsen S, Søndergaard HB, Andresen SR, Magyari M, Sørensen PS, Sellebjerg F, Oturai AB.
Mult Scler Relat Disord. 2019 Aug;33:5-12. doi: 10.1016/j.msard.2019.05.008. Epub 2019 May 16.
31129415
Select item 31060768 6.
Diagnostic Value of Oligoclonal Bands in Children: A Nationwide Population-Based Cohort Study.
Boesen MS, Born AP, Jensen PEH, Sellebjerg F, Blinkenberg M, Lydolph MC, Jørgensen MK, Rosenberg L, Thomassen JQ, Børresen ML.
Pediatr Neurol. 2019 Aug;97:56-63. doi: 10.1016/j.pediatrneurol.2019.03.002. Epub 2019 Mar 13.
31060768
Select item 30944586 7.
Sorensen PS, Sellebjerg F.
Ther Adv Neurol Disord. 2019 Mar 28;12:1756286419836913. doi: 10.1177/1756286419836913. eCollection 2019. Review.
30944586
Select item 30917537 8.
IL-6, IL-12, and IL-23 STAT-Pathway Genetic Risk and Responsiveness of Lymphocytes in Patients with Multiple Sclerosis.
von Essen MR, Søndergaard HB, Petersen ERS, Sellebjerg F.
Cells. 2019 Mar 26;8(3). pii: E285. doi: 10.3390/cells8030285.
30917537
Select item 30877188 9.
Select item 30852181 10.
Perfluorinated substances, risk factors for multiple sclerosis and cellular immune activation.
Ammitzbøll C, Börnsen L, Petersen ER, Oturai AB, Søndergaard HB, Grandjean P, Sellebjerg F.
J Neuroimmunol. 2019 May 15;330:90-95. doi: 10.1016/j.jneuroim.2019.03.002. Epub 2019 Mar 2.
30852181
Select item 30561509 11.
Proinflammatory CD20+ T cells in the pathogenesis of multiple sclerosis.
von Essen MR, Ammitzbøll C, Hansen RH, Petersen ERS, McWilliam O, Marquart HV, Damm P, Sellebjerg F.
Brain. 2019 Jan 1;142(1):120-132. doi: 10.1093/brain/awy301.
30561509
Select item 30515298 12.
The neutrophil-to-lymphocyte ratio is associated with multiple sclerosis.
Hasselbalch IC, Søndergaard HB, Koch-Henriksen N, Olsson A, Ullum H, Sellebjerg F, Oturai AB.
Mult Scler J Exp Transl Clin. 2018 Nov 28;4(4):2055217318813183. doi: 10.1177/2055217318813183. eCollection 2018 Oct-Dec.
30515298
Select item 30513278 13.
Structural and cognitive correlates of fatigue in progressive multiple sclerosis.
Andreasen AK, Iversen P, Marstrand L, Siersma V, Siebner HR, Sellebjerg F.
Neurol Res. 2019 Feb;41(2):168-176. doi: 10.1080/01616412.2018.1547813. Epub 2018 Dec 4.
30513278
Select item 30447419 14.
Jensen PEH, Warnke C, Ingenhoven K, Piccoli L, Gasis M, Hermanrud C, Fernandez-Rodriguez BM, Ryner M, Kramer D, Link J, Ramanujam R, Auer M, Buck D, Grummel V, Bertotti E, Fissolo N, Oliver-Martos B, Nytrova P, Khalil M, Guger M, Rathmaier S, Sievers-Stober C, Lindberg RLP, Hässler S, Bachelet D, Aktas O, Donnellan N, Lawton A, Hemmer B, Havrdova EK, Kieseier B, Hartung HP, Comabella M, Montalban X, Derfuss T, Sellebjerg F, Dönnes P, Pallardy M, Spindeldreher S, Broët P, Deisenhammer F, Fogdell-Hahn A, Sorensen PS; ABIRISK Consortium.
J Neuroimmunol. 2019 Jan 15;326:19-27. doi: 10.1016/j.jneuroim.2018.11.002. Epub 2018 Nov 7.
30447419
Select item 30413632 15.
Select item 30245027 16.
GPR15+ T cells are Th17 like, increased in smokers and associated with multiple sclerosis.
Ammitzbøll C, von Essen MR, Börnsen L, Petersen ER, McWilliam O, Ratzer R, Romme Christensen J, Oturai AB, Søndergaard HB, Sellebjerg F.
J Autoimmun. 2019 Feb;97:114-121. doi: 10.1016/j.jaut.2018.09.005. Epub 2018 Sep 21.
30245027
Select item 30244922 17.
B cells from patients with multiple sclerosis have a pathogenic phenotype and increased LTα and TGFβ1 response.
McWilliam O, Sellebjerg F, Marquart HV, von Essen MR.
J Neuroimmunol. 2018 Nov 15;324:157-164. doi: 10.1016/j.jneuroim.2018.09.001. Epub 2018 Sep 7.
30244922
Select item 30227311 18.
Papp V, Langkilde AR, Blinkenberg M, Schreiber K, Jensen PEH, Sellebjerg F.
Mult Scler Relat Disord. 2018 Nov;26:61-67. doi: 10.1016/j.msard.2018.09.010. Epub 2018 Sep 11.
30227311
Select item 30193769 19.
Inflammatory markers of CHMP2B-mediated frontotemporal dementia.
Roos P, von Essen MR, Nielsen TT, Johannsen P, Stokholm J, Bie AS, Waldemar G, Simonsen AH, Heslegrave A, Zetterberg H; FReJA consortium, Sellebjerg F, Nielsen JE.
J Neuroimmunol. 2018 Nov 15;324:136-142. doi: 10.1016/j.jneuroim.2018.08.009. Epub 2018 Aug 17.
30193769
Select item 30124094 20.
Alcohol consumption in adolescence is associated with a lower risk of multiple sclerosis in a Danish cohort.
Andersen C, Søndergaard HB, Bang Oturai D, Laursen JH, Gustavsen S, Larsen NK, Magyari M, Just-Østergaard E, Thørner LW, Sellebjerg F, Ullum H, Oturai AB.
Mult Scler. 2018 Aug 20:1352458518795418. doi: 10.1177/1352458518795418. [Epub ahead of print]
30124094
Select item 30114292 21.
Select item 30113249 22.
Sellebjerg F, Royen L, Soelberg Sørensen P, Oturai AB, Jensen PEH.
Mult Scler. 2019 Oct;25(11):1444-1451. doi: 10.1177/1352458518794308. Epub 2018 Aug 16.
30113249
Select item 30070595 23.
Petersen ER, Søndergaard HB, Laursen JH, Olsson AG, Börnsen L, Soelberg Sørensen P, Sellebjerg F, Bang Oturai A.
Mult Scler. 2019 Aug;25(9):1298-1305. doi: 10.1177/1352458518791753. Epub 2018 Aug 2.
Select item 30055504 24.
Increased cerebrospinal fluid chitinase 3-like 1 and neurofilament light chain in pediatric acquired demyelinating syndromes.
Boesen MS, Jensen PEH, Magyari M, Born AP, Uldall PV, Blinkenberg M, Sellebjerg F.
Mult Scler Relat Disord. 2018 Aug;24:175-183. doi: 10.1016/j.msard.2018.05.017. Epub 2018 Jun 11.
30055504
Select item 30043661 25.
Dimethyl fumarate therapy suppresses B cell responses and follicular helper T cells in relapsing-remitting multiple sclerosis.
Holm Hansen R, Højsgaard Chow H, Sellebjerg F, Rode von Essen M.
Mult Scler. 2019 Aug;25(9):1289-1297. doi: 10.1177/1352458518790417. Epub 2018 Jul 25.
Select item 29775134 26.
CSF inflammatory biomarkers responsive to treatment in progressive multiple sclerosis capture residual inflammation associated with axonal damage.
Romme Christensen J, Komori M, von Essen MR, Ratzer R, Börnsen L, Bielekova B, Sellebjerg F.
Mult Scler. 2019 Jun;25(7):937-946. doi: 10.1177/1352458518774880. Epub 2018 May 18.
29775134
Select item 29601954 27.
Functional neuroimaging of recovery from motor conversion disorder: A case report.
Dogonowski AM, Andersen KW, Sellebjerg F, Schreiber K, Madsen KH, Siebner HR.
Neuroimage. 2019 Apr 15;190:269-274. doi: 10.1016/j.neuroimage.2018.03.061. Epub 2018 Mar 27. Review.
29601954
Select item 29545067 28.
Effect of natalizumab on disease progression in secondary progressive multiple sclerosis (ASCEND): a phase 3, randomised, double-blind, placebo-controlled trial with an open-label extension.
Kapoor R, Ho PR, Campbell N, Chang I, Deykin A, Forrestal F, Lucas N, Yu B, Arnold DL, Freedman MS, Goldman MD, Hartung HP, Havrdová EK, Jeffery D, Miller A, Sellebjerg F, Cadavid D, Mikol D, Steiner D; ASCEND investigators.
Lancet Neurol. 2018 May;17(5):405-415. doi: 10.1016/S1474-4422(18)30069-3. Epub 2018 Mar 12.
29545067
Select item 29484253 29.
Højsgaard Chow H, Schreiber K, Magyari M, Ammitzbøll C, Börnsen L, Romme Christensen J, Ratzer R, Soelberg Sørensen P, Sellebjerg F.
Brain Behav. 2018 Jan 5;8(2):e00875. doi: 10.1002/brb3.875. eCollection 2018 Feb.
29484253
Select item 29343473 30.
Select item 29336205 31.
Prediction of natalizumab anti-drug antibodies persistency.
Deisenhammer F, Jank M, Lauren A, Sjödin A, Ryner M, Fogdell-Hahn A, Sievers C, Lindberg R, Jensen PE, Sellebjerg F, Christodoulou L, Birchler M, Pallardy M, Auer M, Liblau R; ABIRISK consortium.
Mult Scler. 2019 Mar;25(3):392-398. doi: 10.1177/1352458517753721. Epub 2018 Jan 16.
29336205
Select item 29324249 32.
Disability in progressive MS is associated with T2 lesion changes.
Ammitzbøll C, Dyrby TB, Lyksborg M, Schreiber K, Ratzer R, Romme Christensen J, Iversen P, Magyari M, Garde E, Sørensen PS, Siebner HR, Sellebjerg F.
Mult Scler Relat Disord. 2018 Feb;20:73-77. doi: 10.1016/j.msard.2017.12.010. Epub 2017 Dec 18.
29324249
Select item 29270986 33.
Select item 28831853 34.
Sellebjerg F, Börnsen L, Ammitzbøll C, Nielsen JE, Vinther-Jensen T, Hjermind LE, von Essen M, Ratzer RL, Soelberg Sørensen P, Romme Christensen J.
Mult Scler. 2017 Nov;23(13):1727-1735. doi: 10.1177/1352458517726592. Epub 2017 Aug 23.
28831853
Select item 28778440 35.
Characterization of naïve, memory and effector T cells in progressive multiple sclerosis.
Nielsen BR, Ratzer R, Börnsen L, von Essen MR, Christensen JR, Sellebjerg F.
J Neuroimmunol. 2017 Sep 15;310:17-25. doi: 10.1016/j.jneuroim.2017.06.001. Epub 2017 Jun 3.
Select item 28597127 36.
Select item 28511943 37.
Select item 28427696 38.
Select item 28377586 39.
Systemic frequencies of T helper 1 and T helper 17 cells in patients with age-related macular degeneration: A case-control study.
Sci Rep. 2017 Apr 4;7(1):605. doi: 10.1038/s41598-017-00741-4.
28377586
Select item 28179539 40.
Select item 27919501 41.
Select item 27919484 42.
Select item 27910101 43.
Early safety and efficacy of fingolimod treatment in Denmark.
Voldsgaard A, Koch-Henriksen N, Magyari M, Sellebjerg F, Sørensen PS, Oturai AB.
Acta Neurol Scand. 2017 Jan;135(1):129-133. doi: 10.1111/ane.12573. Epub 2016 Mar 8.
27910101
Select item 27734023 44.
Selected CSF biomarkers indicate no evidence of early neuroinflammation in Huntington disease.
Vinther-Jensen T, Börnsen L, Budtz-Jørgensen E, Ammitzbøll C, Larsen IU, Hjermind LE, Sellebjerg F, Nielsen JE.
Neurol Neuroimmunol Neuroinflamm. 2016 Sep 28;3(6):e287. eCollection 2016 Dec.
27734023
Select item 27645354 45.
Select item 27540591 46.
Select item 27481206 47.
Schreiber K, Magyari M, Sellebjerg F, Iversen P, Garde E, Madsen CG, Börnsen L, Romme Christensen J, Ratzer R, Siebner HR, Laursen B, Soelberg Sorensen P.
Mult Scler. 2017 Apr;23(5):675-685. doi: 10.1177/1352458516661048. Epub 2016 Aug 5.
27481206
Select item 27386506 48.
Absence of systemic oxidative stress and increased CSF prostaglandin F2α in progressive MS.
Lam MA, Maghzal GJ, Khademi M, Piehl F, Ratzer R, Romme Christensen J, Sellebjerg FT, Olsson T, Stocker R.
Neurol Neuroimmunol Neuroinflamm. 2016 Jun 30;3(4):e256. doi: 10.1212/NXI.0000000000000256. eCollection 2016 Aug.
27386506
Select item 27364323 49.
Soelberg Sorensen P, Sellebjerg F.
Mult Scler. 2016 Aug;22(9):1112-3. doi: 10.1177/1352458516658560. Epub 2016 Jun 30. No abstract available.
27364323
Select item 27055806 50.
Koch-Henriksen N, Magyari M, Sellebjerg F, Soelberg Sørensen P.
Mult Scler. 2017 Feb;23(2):234-241. doi: 10.1177/1352458516643393. Epub 2016 Jul 11.
27055806
Sellebjerg F[Author]

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Rabindranath Tagore (film) - Wikipedia
Raya Chatterjee,
Sovanlal Ganguli,
Smaran Ghosal,
Phani Nan,
Rabindranath Tagore is a 1961 black-and-white short film directed by an Indian director Satyajit Ray on the life and works of noted Bengali author Rabindranath Tagore.[1] Ray started working on the documentary in the beginning of 1958 and it was released during the birth centenary year of Rabindranath Tagore, who was born on 7 May 1861.[2] Ray avoided the controversial aspects of Tagore's life in order to make it as an official portrait of the poet. Though Tagore was known as a poet, Ray did not use any of Tagore's poetry as he was not happy with the English translation and believed that "it would not make the right impression if recited" and people would not consider Tagore "a very great poet", based on those translations.[3] Satyajit Ray has been reported to have said about the documentary Rabindranath Tagore in his biography Satyajit Ray: The Inner Eye by W. Andrew Robinson that, "Ten or twelve minutes of it are among the most moving and powerful things that I have produced".[3]
Often regarded as polymath, author of Gitanjali and its "profoundly sensitive, fresh and beautiful verse",[4] Tagore became the first non-European to win the Nobel Prize in Literature in 1913. The first stanza of Tagore's five-stanza Brahmo hymn has been adopted as the National Anthem of India, "Jana Gana Mana".[5] The first ten lines of another Tagore song, "Amar Shonar Bangla" were adopted in 1972 as the Bangladesh's national anthem.[6] Incidentally, Sri Lanka's national anthem "Sri Lanka Matha" was written and composed by Tagore's student, Ananda Samarakoon.[7]
Academy Film Archive, part of the Academy Foundation, took an initiative to restore Satyajit Ray's films and could successfully restore 19 Ray films but Rabindranath Tagore is yet to be restored as its original print was found to be badly damaged.[8] The film's original script was included in a book named Original English Film Scripts Satyajit Ray, put together by Ray's son Sandip Ray.[9]
Rabindranath Tagore was born on 7 May 1861 to Debendranath Tagore and Sarada Devi, the youngest of thirteen surviving children. At the age of seventeen, he was sent to London for higher education, however, he did not finish his studies there. He started a school at Santiniketan which was based on Upanishadic ideals of education.[10] He also participated in the Indian independence movement. Tagore became the first non-European to win the Nobel Prize in Literature in 1913. He was awarded for his collections of poems, Gitanjali (Song Offerings), which included 103 poems with his own English translations of his Bengali poems. In 1915, the British Crown granted Tagore a knighthood. He renounced it after the 1919 Jallianwala Bagh massacre.[11] At the age of 80, Tagore died on 7 August 1941 in his ancestral home in Calcutta.
Narrated by Satyajit Ray, the film begins with the funeral procession of Rabindranath Tagore. Briefly mentioning about Kolkata, then known as "Calcutta", the documentary explains the Tagore lineage, starting with Dwarkanath Tagore. While documentary mentions Dwarkanath Tagore's elder son Debendranath Tagore's association with an Indian religious, social, and educational reformer Raja Rammohun Roy and introduces some of his children out of fourteen, it moves to the birth of child Rabindranath Tagore, fondly called as "Robi". The film then narrates Robi's initial schooling days, his trip to northern India with his father, publication of his first poem in his father's magazine and his failed attempt for higher education at London.
The documentary showcases some of the scenes of Tagore's first drama-opera, Valmiki Pratibha (The Genius of Valmiki), where he used western classical music along with Raga-based songs to narrate sage Valmiki's story and himself acted in the lead role. Mentioning about his marriage with Mrinalini Devi, the documentary explains his aim to form a new school at Santiniketan and its different education system, death of his wife and children in the short span of time and his association in Indian independence movement. It then narrates Tagore's visit to England in 1912 where his English translated poems from Gitanjali were introduced to English painter William Rothenstein, who in-turn showed them to the Irish poet W. B. Yeats. This helped Gitanjali for its publication in England and fetched Tagore the Nobel Prize in Literature in 1913 and a Knighthood in 1915.
While showcasing Tagore's formation of Visva-Bharati University, the documentary mentions his renouncement of his knighthood, in response to the Jallianwala Bagh massacre in 1919. It also documents his world journey for fund collection for his school, his paintings and his 70th birthday where a book, The Golden Book of Tagore, was published with the testimonials by intellectuals of the world, including French dramatist Romain Rolland, German theoretical physicist Albert Einstein, Greek poet Kostis Palamas, Indian Polymath Jagadish Chandra Bose and Indian political leader Mohandas Karamchand Gandhi. The documentary ends while mentioning about Tagore's last days, his last message to the world Civilization in Crisis and his death at his birthplace at the age of 80 on 7 August 1941.
Narrator: Satyajit Ray
Production controller: Anil Chowdhury
Music direction: Jyotirindra Moitra
Make-up: Sakti Sen
Sound recording: Satyen Chatterjee and Durgadas Mitra
After the Academy of Motion Picture Arts and Sciences awarded Satyajit Ray an honorary Academy Award in 1992 for his lifetime achievements,[12] the Academy Film Archive, part of the Academy Foundation which mainly works with the objectives as "preservation, restoration, documentation, exhibition and study of motion pictures", took an initiative to restore and preserve Ray's films.[13] Josef Lindner was appointed as a preservation officer and as of October 2010[update] the Academy has successfully restored 19 titles. However, the documentary Rabindranath Tagore was found to be badly damaged..[8]
Satyajit Ray has been reported to have said about the documentary Rabindranath Tagore in his biography Satyajit Ray: The Inner Eye by W. Andrew Robinson that, "Ten or twelve minutes of it are among the most moving and powerful things that I have produced".[3] At "Ray Festival 2009", Satyajit Ray Society screened Rabindranath Tagore along with other three Ray documentaries, namely Two, The Inner Eye and Sukumar Ray on 7 May 2009. The film was also shown at 51st Valladolid International Film Festival along with other seven Ray films.[14] The film's original script was included in a book named Original English Film Scripts Satyajit Ray, put together by Ray's son Sandip Ray along with an ex-CEO of Ray Society, Aditinath Sarkar, which also included original scripts of Ray's other films.[9][15]
9th National Film Awards (1961): President's Gold Medal for the Best Documentary Film[16]
14th Locarno International Film Festival (1961): Golden Sail, Short Films[17]
Montevideo Film Festival (Uruguay)
Montevideo Film Festival (1962): Special Mention[1]
^ a b "Rabindranath Tagore@satyajitray.org". Retrieved 3 January 2013.
^ "Rabindranath Tagore profile@The Open University". Retrieved 5 January 2013.
^ a b c Robinson, Andrew. "Chapter 26: Documentaries: Sikkim (1971) Sukumar Ray (1987) Bala (1976) Rabindranath Tagore (1961) The Inner Eye (1972)". Satyajit Ray: The Inner Eye. I. B. Tauris; Revised and Updated edition. pp. 278, 279. ISBN 1860649653.
^ "National Anthem of India". Retrieved 6 January 2013.
^ "Bangladesh: Amar Shonar Bangla". NationalAnthems.me. Retrieved 6 January 2013.
^ "Sri Lanka: Sri Lanka Matha". NationalAnthems.me. Retrieved 6 January 2013.
^ a b "Saving a legacy". Retrieved 1 January 2013.
^ a b Nag, Ashoke (9 April 2011). "Satyajit Ray: Saluting the auteur". The Economic Times. Retrieved 1 January 2013.
^ "Rabindranath Tagore profile@nobel". Retrieved 7 January 2013.
^ "Rabindranath Tagore profile@calcuttaweb". Retrieved 7 January 2013.
^ "The 64th Academy Awards (1992)". oscars.org. 30 March 1992. Retrieved 1 January 2013.
^ "About the Academy Film Archive". oscars.org. Retrieved 1 January 2013.
^ "News: Film, Music and Exhibition@satyajitrayworld.com". Retrieved 1 January 2013.
^ "Golden Sail, Short Films". pardo.ch. Retrieved 4 January 2013.
VIAF: 181530634
GND: 4840803-7
Retrieved from "https://en.wikipedia.org/w/index.php?title=Rabindranath_Tagore_(film)&oldid=785575232"

value: This website is the English-language edition of the free online encyclopedia Wikipedia. It was founded on 15 January 2001 as Wikipedia's first edition and, as of October 2021, has the most articles of any edition, at 6,412,521.


text:
French Theater Since 1930, The: Six Contemporary Full-Length Plays by Oreste F., Editor Pucciani: Good Hardcover (2001) First Edition - may be Reissue. | Books Express
Home Oreste F., Editor Pucciani French Theater Since 1930, The: Six Contemporary Full-Length ...
French Theater Since 1930, The: Six Contemporary Full-Length Plays
Oreste F., Editor Pucciani
Published by Blaisdell Publishing Co., 2001
ISBN 10: 0536004498 / ISBN 13: 9780536004499
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Synopsis: Subtitle: Six Contemporary Full-Length Plays
Title: French Theater Since 1930, The: Six ...
1. French Theater Since 1930, The: Six Contemporary Full-Length Plays
Pucciani, Oreste F., Editor
Published by Blaisdell Publishing Co.
ISBN 10: 0536004498 ISBN 13: 9780536004499
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2. French Theater Since 1930, The: Six Contemporary Full-Length Plays
Published by Blaisdell Publishing (1954)
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3. French Theater Since 1930, The: Six Contemporary Full-Length Plays
Book Description Blaisdell Publishing Co. Hardcover. Condition: GOOD. Spine creases, wear to binding and pages from reading. May contain limited notes, underlining or highlighting that does affect the text. Possible ex library copy, thatâ ll have the markings and stickers associated from the library. Accessories such as CD, codes, toys, may not be included. Seller Inventory # 3098238922
4. French Theater Since 1930, The: Six Contemporary Full-Length Plays
Published by Blaisdell Publishing Co. (1954)
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5. The French Theater Since 1930 Six Contemporary Full-Length Plays
Pucciani, Oreste F.; Editor
Published by Xerox College Publishing, Lexington, MA & Toronto
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6. French Theater Since 1930, The: Six Contemporary Full-Length Plays
Book Description Blaisdell Publishing, 1954. Hardcover. Condition: Good. Connecting readers with great books since 1972. Used books may not include companion materials, some shelf wear, may contain highlighting/notes, may not include cdrom or access codes. Customer service is our top priority!. Seller Inventory # S_281847572
7. The French Theater Since 1930 : Six Contemporary Full-Length Plays / Edited by Oreste F. Pucciani
Published by Xerox College Publishing, Toronto (1954)
Book Description Xerox College Publishing, Toronto, 1954. 1954 edition. Near fine copy in the original gilt-blocked cloth. Slightest suggestion only of dust-dulling to the spine bands and panel edges. Remains particularly well-preserved overall; tight, bright, clean and strong. ; 400 pages; Description: ix, 400 p. ; 22 cm. Subjects: French drama--20th century. 1 Kg. Seller Inventory # 69029
8. The French Theater Since 1930 : Six Contemporary Full-Length Plays / Edited by Oreste F. Pucciani
9. French Theater Since 1930, The: Six Contemporary Full-Length Plays [Hardcover] Pucciani, Oreste F.
Book Description Condition: New. New. Seller Inventory # M-0536004498

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