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1. 发明专利

GB190705795A Improvements in and relating to Dressing or Sifting Machines for Potatoes and the like. 未知
公开(公告)号：GB190705795A
公开(公告)日：1907-11-14
申请号：GB190705795D
申请日：1907-03-11
申请人： GORDON ALEXANDER PATERSON
发明人： GORDON ALEXANDER PATERSON
摘要： 5795. Gordon, A. P. March 11. Sifting potatoes &c.-In a machine for sifting or dressing potatoes &c., the materials are fed through a hopper 6, preferably formed in one piece with the riddle case 5 and having an adjustable board 19, on to interchangeable inclined screens 1, 2, 3 of different meshes. The screens are placed in tiers and are supported by adjustable steel straps 24 in the screen case 5, which is suspended by the steel straps 21 from the frame 4 and is reciprocated by manual or other power through gearing 8, a crank-shaft 9, &c. Attached to the front bf the machine and driven from the main shaft at variable speeds is an elevator 12, composed of an endless chain of transverse bars, which transfers the potatoes &c. to the sorting- table 17, or to a weighing-machine, cart, &c. The screens 1, 2 are so arranged that when the screen 1 discharges on to the elevator, the screen 2 discharges into exits 23 having inclined surfaces covered with zinc and vice versa; the screen 3 discharges either to the right or the left of the machine as desired.

2. 发明专利

NZ507937A Improvements relating to the lifting of precast bodies such as concrete panels 未知
公开(公告)号：NZ507937A
公开(公告)日：2001-12-21
申请号：NZ50793799
申请日：1999-05-04
申请人： IAN ALEXANDER PATERSON
发明人： PATERSON IAN ALEXANDER
IPC分类号： E04G21/16 , B66C1/66 , E04G21/14 , B66C1/36 , E04G15/04
摘要： An object handling device includes a support body (32), and an elongate anchor body (40) mounted at the inner end thereof to the support body so as to project from the support body for insertion into an undercut cavity (28) in an object to be handled. At least one anchor lug (48a, 48b) at or adjacent to the outer end of the anchor body is movable with the anchor body between a first position in which the anchor body is able to be inserted into or withdrawn from the cavity, and a second position in which the lug(s) engage respective undercut shoulder portions (29) in the cavity. Means (42) on the anchor body is engagable for moving the anchor body (40) to move the anchor lug(s) between the first and second positions. Lift means (60) on the support body is engagable by a crane to lift the object. Lock means (50, 51) is provided to block movement of the anchor lug(s) from the second position. In one aspect, the anchor body (40) is rotatable to effect a movement of the anchor lug(s). In another, the lock means (50, 51) is slidable generally longitudinally of the anchor body means to a blocking position in which movement of the anchor lug(s) from the second position is blocked. In a further aspect, there is substantially no cavity or void in the object within a region outwards of the undercut shoulder portions (29) sufficient to allow collapse or flow of the object material when the object is being lifted. Also disclosed is a form (25) for defining an undercut cavity in a precast object.

3. 发明专利

GB623632A Improvements relating to the production of motor fuels or constituents 未知
公开(公告)号：GB623632A
公开(公告)日：1949-05-20
申请号：GB1593845
申请日：1945-06-22
申请人： ANGLO IRANIAN OIL CO LTD , ALEXANDER PATERSON SHEARER , LESLIE BENJAMIN WITTEN
IPC分类号： C07C9/16
摘要： In the alkylation of isobutane or isopentane with olefins other than ethylene, for example as described in Specification 479,345, the alkylate is fractionated to recover a fraction containing 2,2,4-trimethylpentane to the exclusion of any of the other isomeric trimethylpentanes, and a fraction containing one or more of the isomers 2,2,3-, 2,3,4- and 2,3,3-trimethylpentanes to the exclusion of 2,2,4-trimethylpentane, and one or other of said fractions is recycled to the alkylation zone whereby products of improved rich or weak mixture performance are obtained as desired. p The alkylate may be separated into cuts of 15-45 DEG , 45-69 DEG , 69-95 DEG , 95-106 DEG and 106-120 DEG C. Recycling part or all of one or more of these fractions gives increased yields of the others. Figures are given to show the effect of adding a 95-106 DEG C. fraction, i.e. 2,2,4-isomer or a 106-120 DEG C. fraction, i.e. 2,2,3-, 2,3,4- and 2,3,3-isomers.

4. 发明专利

GB438062A Fruit and vegetable slicer 未知
公开(公告)号：GB438062A
公开(公告)日：1935-11-11
申请号：GB1573534
申请日：1934-05-26
申请人： JAMES FRANCIS FROST , ALEXANDER PATERSON
IPC分类号： B26B3/03 , B26D3/28
摘要： 438,062. Cutting and slicing vegetables &c. FROST, J. F., Umlaass Farm, and PATERSON, A., Waverley, both in Eston, Natal, South Africa. May 26, 1934, No. 15735. [Class 5 (i)] A device for slicing fruit or vegetables comprises a body portion 1 of wood provided with a V-shaped recess extending from one side to form a slot in the other side, a metal clip 2 holding a safety razor blade 3 being secured to one side of such recess by a screw 4. The clip is slotted to take the screw and adjustment of the blade may be made as the central hole in the blade is larger than the body of the screw. The body portion 1 may be made of sheet metal.

5. 发明专利

AU14702B1 Improvements in trace spreaders 未知
公开(公告)号：AU14702B1
公开(公告)日：1915-09-28
申请号：AU1470214
申请日：1914-10-26
申请人： ALEXANDER PATERSON RENNIE
发明人： ALEXANDER PATERSON RENNIE

6. 发明专利

AU1470214B Improvements in trace spreaders 未知
公开(公告)号：AU1470214B
公开(公告)日：1915-09-28
申请号：AU1470214
申请日：1914-10-26
申请人： ALEXANDER PATERSON RENNIE
发明人： ALEXANDER PATERSON RENNIE

7. 发明专利

GB599906A Improvements relating to the use of liquid alkylation catalysts in the alkylation ofhydrocarbons 未知
公开(公告)号：GB599906A
公开(公告)日：1948-03-24
申请号：GB1555743
申请日：1943-09-22
申请人： ANGLO IRANIAN OIL CO LTD , ALEXANDER PATERSON SHEARER
IPC分类号： C07C2/62
摘要： A process for the alkylation of isoparaffins with olefins other than ethylene to produce hydrocarbons boiling in the motor fuel range, using concentrated sulphuric acid at -10 DEG to 30 DEG C. and sufficient pressure to maintain the liquid phase, and circulating the reaction mixture at a high rate to induce turbulence until the acid concentration is reduced to an extent determined by the quality of the alkylate, comprises charging a reaction zone with fresh acid of high concentration, flowing into said zone a stream of olefin, a substantial excess of isoparaffin, and acid of at least the concentration of that in said zone and at a rate to maintain the acid concentration above the average concentration of the acid in an operational cycle, continuously withdrawing a stream of reaction mixture and conducting at least a portion into a quiescent settlement zone of large capacity wherein the acid is separated, passing said acid to a storage zone of large capacity to accumulate therein a body of acid of average concentration appreciably above that of the acid in the reaction zone, and recycling acid from the storage zone to the reaction zone to serve as "make-up" acid. Using an initial 98 per cent acid, the first period of the operation will yield an alkylate of above standard quality, i.e. the quality obtained with the use of 90 per cent acid. In the second period, acid from the storage zone is used and is discarded while still above 90 per cent. This is used in successive periods until it falls to or below 90 per cent when further use gives a sub-standard alkylate. The process may be continued until the acid is degraded to 85 or even 82 per cent. Part only of the average total acid supplied in an operational cycle may be charged to the alkylator, and to the balance tank or storage zone. The acid in said tank is rapidly circulated to the reaction zone, and additional make-up acid from an external source may be added at such a rate that the total acid, including that originally charged, will not exceed that used in a normal operation. As applied to a single-stage continuous unit, concentrated, e.g. 98 per cent acid, isoparaffin, and olefin are fed by lines e, g, h through pump a where they are emulsified and passed to reactor b. The product separates in settler c, part of the emulsion being recycled by line b1 to maintain an isoparaffin : olefin ratio of 50-150 : 1 or more. Separated acid passes to balance tank d. In the second period, acid is supplied from tank d through pipe c4 and, after separation in settler c, passes to tank d1. In a third period, acid from d1 is used, and separated acid passes to d, and so on. In modifications, the plant is charged with acid, the remainder necessary for an operational cycle is charged to the balance tank, and circulation effected as above or part of the total only is charged and fresh acid added during operation. In multi-stage plants, acid from the settler of one stage passes to the reactor of the next during the initial period, while, in the second period, degraded acid of the first is used as make-up. Degradation of acid in the balance tanks may be prevented by storing in contact with, say, isobutane, which is evaporated to maintain a low temperature. In examples: (1) a continuous multi-stage plant is operated in periods of 10 days; in the first 98 per cent acid is charged and added as make-up, the concentration falling to 95 per cent while the acid withdrawn to the balance tank is 96.5 per cent; in the second, the latter acid is added as make-up, the concentration falling to 92.5 while 94 per cent acid accumulates in a second balance tank; successive periods result in a final concentration of 82 per cent; (2) balance tanks are added and acid drawn entirely therefrom or part charged to the tanks and part added as make-up.

8. 发明专利

GB191411222A Improvements in or relating to Telegraphy. 未知
公开(公告)号：GB191411222A
公开(公告)日：1915-07-01
申请号：GB191411222D
申请日：1914-05-06
申请人： CREED BILLE & CO LTD , ALEXANDER PATERSON OGILVIE
IPC分类号： H04L25/49
摘要： 11,222. Ogilvie, A. P., and Creed, Bille, & Co. May 6. Selective punching and perforating machines.-In a method of perforating a telegraph strip at a distant station, the keys d , e , f , Fig. 3, of a perforating machine are acted on by rubber - shod hammers 20, adjustably connected to the cores 21 of solenoids having two windings 25, 26 arranged to produce consequent poles in their cores. In a modification, the hammer 20 may be connected to a bridge piece connecting the cores of two solenoids. In a further form, the keys d , e , f Fig. 7, may be connected to the solenoid cores 31 through levers 32, compactness being obtained by arranging the solenoids, levers, and keys as shown in Fig. 7.

9. 发明专利

GB611905A Improvements relating to the alkylation of isoparaffins 未知
公开(公告)号：GB611905A
公开(公告)日：1948-11-05
申请号：GB174444
申请日：1944-01-31
申请人： ANGLO IRANIAN OIL CO LTD , ALEXANDER PATERSON SHEARER , THOMAS CUBIN
IPC分类号： C07C7/171
摘要： A pentenes feedstock for use in alkylating isoparaffins is produced by subjecting a pressure distillate obtained in the cracking or reforming distillation of a petroleum containing dienes to refining treatment with sulphuric acid of a concentration lower than that required for use as an alkylation catalyst, and fractionating the refined distillate for recovery of a pentenes fraction. The pressure distillate after debutanization may be treated in a counter-current washer with acid injected at a rate equal to 0.1-1 per cent by volume at a concentration of 85 per cent which is discarded at 45 per cent. Discarded acid from an alkylation process may be used. Temperature may be about atmospheric with a time of about 20 minutes. After neutralizing, the distillate may be passed to a standard re-run unit of three columns where a pentenes fraction is concentrated in a 50 per cent overhead cut from the first, and passes to a re-distillation unit where the pentenes fraction is removed overhead while the bottoms are returned for blending with the cracked spirit from the second and third columns of the re-run unit.ALSO:A pentenes feedstock for use in alkylating isoparaffins is produced by subjecting a pressure distillate obtained in the cracking or reforming distillation of a petroleum containing dienes to refining treatment with sulphuric acid of a concentration lower than that required for use as an alkylation catalyst, and fractionating the refined distillate for recovery of a pentenes fraction. The pressure distillate after debutanization may be treated in a counter-current washer with acid injected at a rate equal to 0.1-1 per cent by volume at a concentration of 85 per cent which is discarded at 45 per cent. Discarded acid from an alkylation process may be used. Temperature may be about atmospheric with a time of about 20 mins. After neutralizing, the distillate may be passed to a standard re-run unit of three columns where a pentenes fraction is concentrated in a 50 per cent overhead cut from the first, and passes to a redistillation unit where the pentenes fraction is removed overhead, while the bottoms is returned for blending with the cracked spirit from the second and third columns of the re-run unit. The fraction may be used to alkylate isoparaffins with sulphuric acid of above 85 per cent, an acid : hydrocarbon ratio of 1 : 1, external ratio of isoparaffin : olefin up to 9 : 1 or more, and contact-time of 20-80 mins. at 35-65 DEG F. Examples show the saving in acid consumption during alkylation, using a pentenes feed prepared as above as compared with feeds pretreated by known processes or untreated. Specification 599,906 is referred to.

10. 发明专利

GB600468A Improvements in the production and recovery of isoparaffins, more particularly isopentanes 未知
公开(公告)号：GB600468A
公开(公告)日：1948-04-09
申请号：GB2282744
申请日：1944-11-17
申请人： ANGLO IRANIAN OIL CO LTD , ALEXANDER PATERSON SHEARER , THOMAS CUBIN
摘要： A debutanized straight-run distillate from crude petroleum is fractionated to separate isoparaffins from residual normal hydrocarbons which are then thermally reformed and the product fractionated to recover a pressure distillate, C1-C4 hydrocarbons, and a residue fraction, said pressure distillate being fractionated to recover a C5 fraction containing pentane, isopentane and olefins, alkylating isobutane with the said fraction in the presence of sulphuric acid, fractionating to obtain an isobutane fraction, a C5 fraction and an alkylate fraction, and fractionating the C5 fraction to recover isopentane. During the alkylation of isobutane with the olefinic C5 fraction using sulphuric acid as catalyst, for example as described in Specification 479,345, it is found that isopentane is produced. In an example, a petroleum distillate of B.R. 25-125 DEG C. is superfractionated to recover isopentane, isohexane and isoheptane fractions, the residue being reformed, a C5 fraction separated, alkylated with isobutane in liquid phase using 85 per cent sulphuric acid at 10 DEG C., and a separated pentane fraction superfractionated to recover isopentane while n-pentane is recycled to the reforming stage.

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