CSCE 430/830 Computer Architecture Basic Pipelining & Performance Adopted from Professor David Patterson Electrical Engineering and Computer Sciences University of California, Berkeley Outline • • • • • • • MIPS – An ISA for Pipelining 5 stage pipelining Structural and Data Hazards Forwarding Branch Schemes Exceptions and Interrupts Conclusion 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 2 A "Typical" RISC ISA • • • • 32-bit fixed format instruction (3 formats) 32 32-bit GPR (R0 contains zero, DP take pair) 3-address, reg-reg arithmetic instruction Single address mode for load/store: base + displacement – no indirection • Simple branch conditions • Delayed branch see: SPARC, MIPS, HP PA-Risc, DEC Alpha, IBM PowerPC, CDC 6600, CDC 7600, Cray-1, Cray-2, Cray-3 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 3 Example: MIPS ( MIPS) Register-Register 31 26 25 Op 21 20 Rs1 16 15 Rs2 11 10 6 5 Rd 0 Opx Register-Immediate 31 26 25 Op 21 20 Rs1 16 15 Rd immediate 0 Branch 31 26 25 Op Rs1 21 20 16 15 Rs2/Opx immediate 0 Jump / Call 31 26 25 Op 7/27/2016 target CSCE 430/830, Basic Pipelining & Performance 0 4 Datapath vs Control Datapath Controller signals Control Points • Datapath: Storage, FU, interconnect sufficient to perform the desired functions – Inputs are Control Points – Outputs are signals • Controller: State machine to orchestrate operation on the data path – Based on desired function and signals 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 5 Approaching an ISA • Instruction Set Architecture – Defines set of operations, instruction format, hardware supported data types, named storage, addressing modes, sequencing • Meaning of each instruction is described by RTL (Register Transfer Language) on architected registers and memory • Given technology constraints assemble adequate datapath – – – – Architected storage mapped to actual storage Function units to do all the required operations Possible additional storage (eg. MAR, MBR, …) Interconnect to move information among regs and FUs • Map each instruction to sequence of RTLs • Collate sequences into symbolic controller state transition diagram (STD) • Lower symbolic STD to control points • Implement controller 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 6 5 Steps of MIPS Datapath Figure A.2, Page A-8 Instruction Fetch Instr. Decode Reg. Fetch Execute Addr. Calc Next SEQ PC Adder 4 Zero? RS1 L M D MUX Data Memory ALU Imm MUX MUX RD Reg File Inst Memory Address IR <= mem[PC]; RS2 Write Back MUX Next PC Memory Access Sign Extend PC <= PC + 4 Reg[IRrd] <= Reg[IRrs1] opIRop Reg[IRrs2] 7/27/2016 WB Data CSCE 430/830, Basic Pipelining & Performance 7 5 Steps of MIPS Datapath Figure A.3, Page A-9 Execute Addr. Calc Instr. Decode Reg. Fetch Next SEQ PC Next SEQ PC Adder 4 Zero? RS1 MUX MEM/WB Data Memory EX/MEM A <= Reg[IRrs1]; Imm ALU PC <= PC + 4 MUX MUX IR <= mem[PC]; ID/EX RD Reg File IF/ID Memory Address RS2 Write Back MUX Next PC Memory Access WB Data Instruction Fetch Sign Extend RD RD RD B <= Reg[IRrs2] rslt <= A opIRop B WB <= result 7/27/2016 Reg[IRrd] <= WB CSCE 430/830, Basic Pipelining & Performance 8 Inst. Set Processor Controller IR <= mem[PC]; PC <= PC + 4 JSR A <= Reg[IRrs1]; JR br if bop(A,b) Ifetch opFetch-DCD ST B <= Reg[IRrs2] jmp RR PC <= IRjaddr r <= A opIRop B RI LD r <= A opIRop IRim r <= A + IRim WB <= r WB <= Mem[r] PC <= PC+IRim WB <= r Reg[IRrd] <= WB Reg[IRrd] <= WB CSCE 430/830, Basic Pipelining & Performance Reg[IRrd] <= WB 9 5 Steps of MIPS Datapath Figure A.3, Page A-9 Execute Addr. Calc Instr. Decode Reg. Fetch Next SEQ PC Next SEQ PC Adder 4 Zero? RS1 MUX MEM/WB Data Memory EX/MEM ALU MUX MUX ID/EX Imm Reg File IF/ID Memory Address RS2 Write Back MUX Next PC Memory Access WB Data Instruction Fetch Sign Extend RD RD RD • Data stationary control – local 7/27/2016 decode CSCE for each instruction phase / pipeline stage 430/830, Basic Pipelining & Performance 10 Visualizing Pipelining Figure A.2, Page A-8 Time (clock cycles) 7/27/2016 Reg DMem Ifetch Reg DMem Reg ALU DMem Reg ALU O r d e r Ifetch ALU I n s t r. ALU Cycle 1 Cycle 2 Cycle 3 Cycle 4 Cycle 5 Cycle 6 Cycle 7 Ifetch Ifetch Reg Reg CSCE 430/830, Basic Pipelining & Performance Reg DMem Reg 11 Instruction-Level Parallelism • Review of Pipelining (the laundry analogy) 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 12 Pipelining is not quite that easy! • Limits to pipelining: Hazards prevent next instruction from executing during its designated clock cycle – Structural hazards: HW cannot support this combination of instructions (single person to fold and put clothes away) – Data hazards: Instruction depends on result of prior instruction still in the pipeline (missing sock) – Control hazards: Caused by delay between the fetching of instructions and decisions about changes in control flow (branches and jumps). 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 13 One Memory Port/Structural Hazards Figure A.4, Page A-14 Time (clock cycles) 7/27/2016 Reg DMem Reg DMem Reg DMem Reg ALU Instr 4 Ifetch ALU Instr 3 DMem ALU O r d e r Instr 2 Reg ALU I Load Ifetch n s Instr 1 t r. ALU Cycle 1 Cycle 2 Cycle 3 Cycle 4 Cycle 5 Cycle 6 Cycle 7 Ifetch Ifetch Reg Ifetch Reg CSCE 430/830, Basic Pipelining & Performance Reg Reg Reg DMem 14 One Memory Port/Structural Hazards (Similar to Figure A.5, Page A-15) Time (clock cycles) Stall DMem Ifetch Reg DMem Reg ALU Ifetch Bubble Instr 3 Reg Reg DMem Bubble Bubble Ifetch Reg Reg Bubble ALU O r d e r Instr 2 Reg ALU I Load Ifetch n s Instr 1 t r. ALU Cycle 1 Cycle 2 Cycle 3 Cycle 4 Cycle 5 Cycle 6 Cycle 7 Bubble Reg DMem How do you “bubble” the pipe? 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 15 Speed Up Equation for Pipelining CPIpipelined Ideal CPI Average Stall cycles per Inst Cycle Timeunpipelined Ideal CPI Pipeline depth Speedup Ideal CPI Pipeline stall CPI Cycle Timepipelined For simple RISC pipeline, CPI = 1: Cycle Timeunpipelined Pipeline depth Speedup 1 Pipeline stall CPI Cycle Timepipelined 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 16 Example: Dual-port vs. Single-port • Machine A: Dual ported memory (“Harvard Architecture”) • Machine B: Single ported memory, but its pipelined implementation has a 1.05 times faster clock rate • Ideal CPI = 1 for both • Loads are 40% of instructions executed SpeedUpA = Pipeline Depth/(1 + 0) x (clockunpipe/clockpipe) = Pipeline Depth SpeedUpB = Pipeline Depth/(1 + 0.4 x 1) x (clockunpipe/(clockunpipe / 1.05) = (Pipeline Depth/1.4) x 1.05 = 0.75 x Pipeline Depth SpeedUpA / SpeedUpB = Pipeline Depth/(0.75 x Pipeline Depth) = 1.33 • Machine A is 1.33 times faster 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 17 Data Hazard on R1 Figure A.6, Page A-17 Time (clock cycles) and r6,r1,r7 or r8,r1,r9 xor r10,r1,r11 7/27/2016 Ifetch DMem Reg DMem Ifetch Reg DMem Ifetch Reg DMem Ifetch Reg ALU sub r4,r1,r3 Reg ALU Ifetch ALU O r d e r add r1,r2,r3 WB ALU I n s t r. MEM ALU IF ID/RF EX Reg CSCE 430/830, Basic Pipelining & Performance Reg Reg Reg DMem 18 Reg Three Generic Data Hazards • Read After Write (RAW) InstrJ tries to read operand before InstrI writes it I: add r1,r2,r3 J: sub r4,r1,r3 • Caused by a “Dependence” (in compiler nomenclature). This hazard results from an actual need for communication. 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 19 Three Generic Data Hazards • Write After Read (WAR) InstrJ writes operand before InstrI reads it I: sub r4,r1,r3 J: add r1,r2,r3 K: mul r6,r1,r7 • Called an “anti-dependence” by compiler writers. This results from reuse of the name “r1”. • Can it happen in MIPS 5 stage pipeline? – All instructions take 5 stages, and – Reads are always in stage 2, and – Writes are always in stage 5 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 20 Three Generic Data Hazards • Write After Write (WAW) InstrJ writes operand before InstrI writes it. I: sub r1,r4,r3 J: add r1,r2,r3 K: mul r6,r1,r7 • Called an “output dependence” by compiler writers This also results from the reuse of name “r1”. • Can’t happen in MIPS 5 stage pipeline because: – All instructions take 5 stages, and – Writes are always in stage 5 • Will see WAR and WAW in more complicated pipes 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 21 Forwarding to Avoid Data Hazard Figure A.7, Page A-19 or r8,r1,r9 xor r10,r1,r11 7/27/2016 Reg DMem Ifetch Reg DMem Ifetch Reg DMem Ifetch Reg ALU and r6,r1,r7 Ifetch DMem ALU sub r4,r1,r3 Reg ALU O r d e r add r1,r2,r3 Ifetch ALU I n s t r. ALU Time (clock cycles) Reg Reg CSCE 430/830, Basic Pipelining & Performance Reg Reg DMem 22 Reg HW Change for Forwarding Figure A.23, Page A-37 NextPC mux MEM/WR EX/MEM ALU mux ID/EX Registers Data Memory mux Immediate What circuit detects and resolves this hazard? 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 23 Forwarding to Avoid LW-SW Data Hazard Figure A.8, Page A-20 or r8,r6,r9 xor r10,r9,r11 Reg DMem Ifetch Reg DMem Ifetch Reg DMem Ifetch Reg ALU sw r4,12(r1) Ifetch DMem ALU lw r4, 0(r1) Reg ALU O r d e r add r1,r2,r3 Ifetch ALU I n s t r. ALU Time (clock cycles) Reg Reg Reg Reg DMem Any hazard that cannot be avoided with forwarding? 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 24 Reg Data Hazard Even with Forwarding Figure A.9, Page A-21 and r6,r1,r7 or 7/27/2016 r8,r1,r9 DMem Ifetch Reg DMem Reg Ifetch Ifetch Reg Reg CSCE 430/830, Basic Pipelining & Performance Reg DMem ALU O r d e r sub r4,r1,r6 Reg ALU lw r1, 0(r2)Ifetch ALU I n s t r. ALU Time (clock cycles) Reg Reg DMem 25 Data Hazard Even with Forwarding (Similar to Figure A.10, Page A-21) and r6,r1,r7 or r8,r1,r9 7/27/2016 Reg DMem Ifetch Reg Bubble Ifetch Bubble Reg Bubble Ifetch Reg CSCE 430/830, Basic Pipelining & Performance How is this detected? DMem Reg Reg Reg DMem ALU sub r4,r1,r6 Ifetch ALU O r d e r lw r1, 0(r2) ALU I n s t r. ALU Time (clock cycles) DMem 26 Software Scheduling to Avoid Load Hazards Try producing fast code for a = b + c; d = e – f; assuming a, b, c, d ,e, and f in memory. Slow code: LW LW ADD SW LW LW SUB SW Rb,b Rc,c Ra,Rb,Rc a,Ra Re,e Rf,f Rd,Re,Rf d,Rd Fast code: LW LW LW ADD LW SW SUB SW Rb,b Rc,c Re,e Ra,Rb,Rc Rf,f a,Ra Rd,Re,Rf d,Rd Compiler optimizes for performance. Hardware checks for safety. 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 27 Outline • • Review Quantify and summarize performance – Ratios, Geometric Mean, Multiplicative Standard Deviation • • • • • • • • F&P: Benchmarks age, disks fail,1 point fail danger MIPS – An ISA for Pipelining 5 stage pipelining Structural and Data Hazards Forwarding Branch Schemes Exceptions and Interrupts Conclusion 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 28 r6,r1,r7 22: add r8,r1,r9 Ifetch Reg DMem Ifetch Reg DMem Ifetch Reg DMem Ifetch Reg ALU 18: or DMem ALU 14: and r2,r3,r5 Reg ALU Ifetch ALU 10: beq r1,r3,36 ALU Control Hazard on Branches Three Stage Stall 36: xor r10,r1,r11 Reg Reg Reg Reg DMem What do you do with the 3 instructions in between? How do you do it? Where is the “commit”? 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 29 Reg Branch Stall Impact • If CPI = 1, 30% branch, Stall 3 cycles => new CPI = 1.9! • Two part solution: – Determine branch outcome sooner, AND – Compute taken branch (target) address earlier • MIPS branch tests if register = 0 or 0 • MIPS Solution: – Move Zero test to ID/RF stage – Adder to calculate new PC in ID/RF stage – 1 clock cycle penalty for branch versus 3 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 30 Pipelined MIPS Datapath Figure A.24, page A-38 Instruction Fetch Memory Access Write Back Adder Adder MUX Next SEQ PC Next PC Zero? RS1 MUX MEM/WB Data Memory EX/MEM ALU MUX ID/EX Imm Reg File IF/ID Memory Address RS2 WB Data 4 Execute Addr. Calc Instr. Decode Reg. Fetch Sign Extend RD RD RD • Interplay of instruction set design and cycle time. 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 31 Four Branch Hazard Alternatives #1: Stall until branch direction is clear #2: Predict Branch Not Taken – – – – – Execute successor instructions in sequence “Squash” instructions in pipeline if branch actually taken Advantage of late pipeline state update 47% MIPS branches not taken on average PC+4 already calculated, so use it to get next instruction #3: Predict Branch Taken – 53% MIPS branches taken on average – But haven’t calculated branch target address in MIPS » MIPS still incurs 1 cycle branch penalty » Other machines: branch target known before outcome 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 32 Four Branch Hazard Alternatives #4: Delayed Branch – Define branch to take place AFTER a following instruction branch instruction sequential successor1 sequential successor2 ........ sequential successorn branch target if taken Branch delay of length n – 1 slot delay allows proper decision and branch target address in 5 stage pipeline – MIPS uses this 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 33 Scheduling Branch Delay Slots (Fig A.14) A. From before branch add $1,$2,$3 if $2=0 then delay slot becomes B. From branch target sub $4,$5,$6 add $1,$2,$3 if $1=0 then delay slot becomes if $2=0 then add $1,$2,$3 add $1,$2,$3 if $1=0 then sub $4,$5,$6 C. From fall through add $1,$2,$3 if $1=0 then delay slot sub $4,$5,$6 becomes add $1,$2,$3 if $1=0 then sub $4,$5,$6 • A is the best choice, fills delay slot • In B, the sub instruction may need to be copied, increasing IC • In B and C, must be okay to execute sub when branch fails 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 34 Delayed Branch • Compiler effectiveness for single branch delay slot: – Fills about 60% of branch delay slots – About 80% of instructions executed in branch delay slots useful in computation – About 50% (60% x 80%) of slots usefully filled • Delayed Branch downside: As processor go to deeper pipelines and multiple issue, the branch delay grows and need more than one delay slot – Delayed branching has lost popularity compared to more expensive but more flexible dynamic approaches – Growth in available transistors has made dynamic approaches relatively cheaper 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 35 Evaluating Branch Alternatives Pipeline speedup = Pipeline depth 1 +Branch frequency Branch penalty Assume 4% unconditional branch, 6% conditional branchuntaken, 10% conditional branch-taken Scheduling Branch CPI speedup v. speedup v. scheme penalty unpipelined stall Stall pipeline 3 1.60 3.1 1.0 Predict taken 1 1.20 4.2 1.33 Predict not taken 1 1.14 4.4 1.40 Delayed branch 0.5 1.10 4.5 1.45 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 36 More branch evaluations • Suppose the branch frequencies (as percentage of all instructions) of 15% cond. Branches, 1% jumps and calls, and 60% cond. Branches are taken. Consider a 4-stage pipeline where branch is resolved at the end of the 2nd cycle for uncond. Branches and at the end of the 3rd cycle for cond. Branches. How much faster would the machine be without any branch hazards, ignoring other pipeline stalls? Pipeline speedupideal = Pipeline depth/(1+Pipeline stalls) = 4/(1+0) = 4 Pipeline stallsreal = (1x1%) + (2x9%) + (1x6%) = 0.24 Pipeline speedupreal = 4/(1+0.24) = 3.23 Pipeline speedupwithout control hazards = 4/3.23 = 1.24 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 37 More branch question • A reduced hardware implementation of the classic 5-stage RISC pipeline might use the EX stage hardware to perform a branch instruction comparison and then not actually deliver the branch target PC to the IF stage until the clock cycle in which the branch reaches the MEM stage. Control hazard stalls can be reduced by resolving branch instructions in ID, but improving performance in one aspect may reduce performance in other circumstances. • How does determining branch outcome in the ID stage have the potential to increase data hazard stall cycles? 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 38 Problems with Pipelining • Exception: An unusual event happens to an instruction during its execution – Examples: divide by zero, undefined opcode • Interrupt: Hardware signal to switch the processor to a new instruction stream – Example: a sound card interrupts when it needs more audio output samples (an audio “click” happens if it is left waiting) • Problem: It must appear that the exception or interrupt must appear between 2 instructions (Ii and Ii+1) – The effect of all instructions up to and including Ii is totally complete – No effect of any instruction after Ii can take place • The interrupt (exception) handler either aborts program or restarts at instruction Ii+1 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 39 Precise Exceptions in Static Pipelines Key observation: architected state only change in memory and register write stages. 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 40 And In Conclusion: Control and Pipelining • Quantify and summarize performance – Ratios, Geometric Mean, Multiplicative Standard Deviation • • • • • F&P: Benchmarks age, disks fail,1 point fail danger Next time: Read Appendix A, record bugs online! Control VIA State Machines and Microprogramming Just overlap tasks; easy if tasks are independent Speed Up Pipeline Depth; if ideal CPI is 1, then: Cycle Timeunpipelined Pipeline depth Speedup 1 Pipeline stall CPI Cycle Timepipelined • Hazards limit performance on computers: – Structural: need more HW resources – Data (RAW,WAR,WAW): need forwarding, compiler scheduling – Control: delayed branch, prediction • Exceptions, Interrupts add complexity • Next time: Read Appendix C, record bugs online! 7/27/2016 CSCE 430/830, Basic Pipelining & Performance 41